United States
Environmental Protection
Agency
Office of Water
& Waste Management
Washington DC 20460
(SW-789)
1979
Fourth United States-Japan
Governmental Conference
on Solid Waste
Management
March 12-13,1979

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                 FOURTH

         UNITED  STATES-JAPAN

       GOVERNMENTAL  CONFERENCE

      ON SOLID WASTE MANAGEMENT

 MARCH 12-13,  1979,  WASHINGTON, D.C.
      This conference  was hosted
    by the Office  of  Solid Waste,
U.S. Environmental  Protection Agency.
               U.S. Er.vlr•-.-..••'

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                              CONTENTS
 Introduction	     1

 Welcoming Remarks
 (by Dr.  John H.  Skinner, U.S. Chairman)	     4

 Welcoming Remarks
 (by Tadayuki Morishita, Japan Chairman)	     6

 1.   Status Report of Solid Waste Mangement
     1.1   U.S. Paper:  Status of the Solid Waste
          Effort  in the U.S.  (by John W. Thompson)	     8

     1.2   Japan Papers:
          1.2.1  Solid Waste  Management in Japan
                 (by Mr. Tadayuki Morishita)	    25

          1.2.2  Current State of Pneumatic Conveying
                 Systems of Domestic Waste (by Mr. Akio
                 Namiki)	    52

          1.2.3  Location Problems of Refuse Treatment
                 Facilities (by Dr. Shiro Kawaguchi)	    73

          1.2.4  Remvoing HCL Gas in the Exhaust from a
                 Refuse Incineration Plant - A Case of
                 Yokohama City (by Mr. Takashi
                 Miyanohara	    90

2.   Environmental Assessment  for Land Disposal
    2.1   U.S. Paper:  Guidelines for the Land Disposal
         of Solid Waste (by Mr. Truett V. DeGeare, Jr.)..   117

    2.2   Japan Paper:  Environmental Assessment from the
         Viewpoint of Solid Waste Management (by Dr.
         Masaru Tanaka )..	   163

3.   Leachate Control and Treatment
    3.1   U.S. Paper:  Leachate Treatment Demonstration
         (by Mr.  Bernard J. Stoll)	   199

    3.2   Leachate Treatment at Solid Waste Disposal
         Site (presented by Mr. Tadayuki Morishita)	   217

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4.   Resource Recovery Technologies and Markets
    4.1  Japan Papers:
         4.1.1  Recycling of Municipal Waste in Japan
                (presented by Mr.  Tadayuki Morishita)...    234

         4.1.2  An Effective Use of Waste Heat of
                Refuse  Incineration - The Experience
                of Sapporo City (by Mr. Fujio Oikawa
                and Mr.  Hiroto Mitani)	    260

         4.1.3  Composting System:  Part I
                (by Dr.  Sachiho Naito)	    305

         4.1.4  Composting System:  Part II
                (by Mr.  ShigeruAoki)	    333

         4.1.5  Source  Separation for Resource Recovery -
                State of the Art (by Mr. Sukehiro Gotoh,
                Mr. Eiji Tanaka, and Mr Yoichi Yonemura).  357

         4.1.6  Economic Incentives for Municipal Waste
                Collection and Recovery in Japan
                (by Organization for Economic Cooperation
                and Development, Environment Dictorate...  396

    4.2  U.S. Papers:

         4.2.1  State Solid Waste Management Plans
                (by Mr.  George A.  Garland)	  430

         4.2.2  Markets  for Recovered Materials, A Current
                Overview (by Mr. Albert A. Peter, Jr.)...  440

5.   Pyrolysis
    5.1  U.S. Paper:  The Recovery of Energy from
         Municipal Solid Waste (A Review of Activity in
         the United States (by Mr. David B. Sussman and
         Mr. Steven J.  Levy)	   469

    5.2  Japan Papers:
         5.2.1  R and D  of Resource Recovery Systems
                (by Mr.  Hideaki Takamatsu)	   521

         5.2.2  Two-Bed  Type Pyrolysis
                (by Mr.  Kideaki Takamatsu)	   539

         5.2.3  Fluidized Bed Pyrolysis
                (by Mr.  Kideaki Takamatsu)	   553

         5.2.4  R and D  for High Temperature Melting
                of Incombustin and Refuse Unit for
                Incineration (by Dr. Naomichi Hirayama)..   580
                              ii

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Summary Comments, Japan Government
(by Mr. Tadayuki Morishita, Japan Chairman)....	  596

Summary Comments, U.S. Government
(by Dr. John H. Skinner, U.S. Chairman)	  599

Summary of Results and Conclusions	  602

Joint Communique	  606
                         iii

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                          INTRODUCTION









     The Fourth United States-Japan Governmental Conference on




Solid Waste Management was held in Washington, D.C., beginning




March 12, 1979.  The formal, scientific meetings were held on




March 12 and 13 at the American Public Health Association




headquarters.   These meetings were followed by site visits in




the Washington metropolitan area, New York, Louisiana, Mississippi,




Arizona, and California; the visits were concluded on March 23,




1979.




     These bilaterial meetings are an outgrowth of decisions




made at the Second United States-Japan Ministerial Conference




on Pollution Control held in Washington, D.C., in 1974.  The




First Conference on Solid Waste Management was held in Japan in




1973 followed by a second conference in Washington in 1974.




The third meeting took place in Japan in 1976.  While the first




two conferences focused attention on policy issues related to




solid waste management, the third gave priority to specific




solid waste management technical problems.




     The Fourth U.S.-Japan Governmental Conference exchanged




information on three principal areas of solid waste management:




Environmenal Assessment for Land Disposal, Leachate Control and




Treatment, and Resource Recovery Technologies.  Scientific




papers were circulated in advance as were questions posed by




each delegation regarding the other delegation's papers.  Each




conference participant presented a 10 minute overview of his

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paper, which was followed by 20 minutes devoted to discussion

and answering questions on the paper.

     The Japanese delegation, headed by Mr. Tadayuki Morishita,

Director, Waste Management Division, Water Supply and Environmental

Sanitation Department, Environmental Health Bureau, Ministry of

Health and Welfare, was composed of four national government

officials, two local government officials and four other

representatives from research or academic institutes, and three

observers.

     The U.S delegation, headed by Dr.  John Skinner, Director

of State Programs & Resource Recovery Division, Office of Solid

Waste, U.S. Environmental Protection Agency, was composed of

ten EPA officials.   Various representatives from other Federal

agencies and public interest groups were also in attendance.

     Following the  two days of formal meetings, the Japanese

delegates visited the following eight solid waste management

and resource recovery facilities:



        Beltsville  Sludge Project, Metropolitan Washington, D.C.

        Hempstead Wet Pulping Facility, Hempstead, New York

        Resource Recovery I Project, New Orleans, Louisiana

        Corps of Engineers' Waterways Experiment Station
                            Vicksburg,  Mississippi

        City of Phoenix Sanitation Plant, Phoenix, Arizona

        I.T. Environmental Corporatoin (Hazardous Waste Facility)
                            San Francisco, California

        Mountain View Methane Gas Recovery (Pacific Gas and
               Electric Company),  San Francisco, California

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     This publication includes the papers prepared for the




conference as well as the Welcoming Remarks and Summary Comments




presented by both Chairmen, the Summary of Resoults and




Conclusions, and the Joint Communique.  Also included are the




question-and-answer sessions which followed each presentation.




These discussions sessions have been transcribed from tape




recordings of the conference and are presented with only minimal




editing for clarity.

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                        Welcoming Remarks
               Dr. John H.  Skinner, U.S. Chairman
Dr. Skinner:  Good morning.  I would like to welcome everyone to the
Fourth Governmental Conference on Solid Waste Management between the
United States and Japan.  My name is John Skinner and I am the United
States Chairman for this conference.  I would like to introduce to our
American guests, Mr. Morishita, who is the Japanese Chairman for this
conference.  I will be chairing this conference today and Mr. Morishita
will be handling the chairmanship tomorrow.
     These conferences began in 1973.  Two conferences have been held in
Japan and this is the second one held in the United States.  One of the
greatest benefits of this conference is the informal exchange between
our two nations and we hope to continue that exchange today and tomorrow.
     If you look in the information packet of materials you received for
the conference, you will find an agenda.  This is the order in which
the papers will be presented.  Each paper will be summarized in approxi-
mately five minutes, including the translation, after which there will
be questions asked by the other delegation.  Questions may then be
posed by the other guests in the room.  Each discussion topic should
take approximately thirty minutes.
     There have been some major changes in solid waste management in
the United States since our last meeting in large part attributed to the
passage of a new federal law entitled "The Resource Conservation and
Recovery Act."  This new law has established many new federal programs
in the area of hazardous waste management, land disposal, resource recovery

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 and conservation.   We  are very  happy  to be  able  to  share  some  of  our



 experiences  in  carrying out  our new programs  under  this law.



      On  the  last page  of the Agenda there is  a listing of the  site



 visits that  we  have arranged for you  following the  two days of formal




 meetings in  Washington.   Over the  next  week you  will  be visiting  some



 of  the newest and  most interesting solid waste management facilities




 in  the United States.



      Again,  on  behalf  of the United States  and on behalf  of the Environ-



 mental Protection  Agency,  I  would  like  to offer  you my warm welcome and



 my  best  wishes  for a very successful  and productive conference.   Our



 delegates were  honored by the friendship and  hospitality  of the Japanese



 people when  they visited Japan  and I  hope that we can reciprocate while



 you are  in our  country.
     Chairman Skinner then  introduced the United States delegation and



 guests.  He also noted that the conference papers and the questions and



answers will be distributed  to all participants within approximately two



 months.

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                       Welcoming Remarks
               Mr. Tadayuki Morishita, Japan Chairman

Mr. Morishita:  Thank you so much for your remarks about this conference.
First of all, I would like to take this opportunity to make some welcoming
remarks.  I understand that the United States has been making a continuous
effort to protect its environment, especially in the field of solid
waste management.  So we believe that we have a lot to learn from you.
I would also like to take this opportunity to express our thanks and
appreciation for making it possible for us to participate in this
United States-Japan Solid Waste Management Conference.
     Since the last G-overnmental Solid Waste Management Conference held in
May 1976, we have introduced an amendment to the Japan Waste Disposal Act
to strengthen our regulations against the people who are responsible for
the discharge of solid waste.  We also have strengthened the supervision
of waste management activities in municipalities.  In addition,  we have
introduced some measures to subsidize some municipalities in order to
enhance efforts in finding sites for sanitary land fills for municipal
waste.  Our country has started some pilot projects in the areas of
solid waste resource recovery and pneumatic collection of waste.  We will
be introducing reports on these projects during this conference.
     On the other hand, in the United States in 1976,  we understand you
enacted the Resource Conservation and Recovery Act to protect the public's
health and environmental quality in terms of enhancement through the
proper management of solid waste.  We have a high regard for your efforts
to get into a field of source separation.

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     In Japan, we wrestle with resource recovery from waste and recycling




of waste from the perspective of waste reduction.  However, even though




we are known as a prosperous nation, full of resources, still we wrestle




with this solid waste management problem from the broad prospective of




the protection of the environment.  Thus we would like to express a




great respect for your efforts.  For this conference, we have brought




our best experts in solid waste management and even though we have a




very limited amount of time, we are hoping to have a smooth exchange




of good information in terms of solid waste management.  By doing so, we




are hoping to promote better programs in the U.S. and Japan to protect




our environments  and in the long run protect the public's health.
Chairman Morishita then introduced the members of the Japanese delegation.

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        STATUS OF THE SOLID WASTE EFFORT IN THE



                     UNITED STATES





     In preparing for this paper on the status of the



U.S. solid waste program, I looked back at what we were



doing just two and one half years ago.  Essentially, it



consisted of:



     1.   Financial aid to State programs totaling about $3



          million a year, accompanied by technical assistance;








     2.   Technology research, such as the design of collection,



          processing, and disposal equipment;








     3.   System research, such as collection sched-uling and



          routing, cost analysis, and study of the impact of



          solid waste policies;








     4.   Demonstration projects—the actual trials of



          various disposal and resource recovery options;







     5.   Analyses of resource recovery and waste reduction,



          which were reported annually to the Congress;








     6.   The study of hazardous waste problems and their



          control; and





                  A Paper by John W.  Thompson



                     Local Program Manager



                  Land Disposal  Division



                   Office of Solid Waste,  EPA

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     7.   Development of recommended guidelines.







     The program was concerned mainly with developing ways



to improve the management of municipal solid waste, hazardous



waste management was a new field, and we had no legal



authority to develop and implement regulations for managing



solid wastes.








     On October 21, 1976, our basic legislation, the Solid



Waste Disposal Act, was amended by the Resource Conservation



and Recovery Act of 1976, Public Law 94-580.  The new



legislation reflected a greatly expanded awareness of



environmental and health problems associated with improper



disposal of solid waste.







     The passage of RCRA signified that our nation was now



ready to face the fact that land is a natural medium which



needs to be protected just as air and water do, and that



resource conservation and recovery are key elements in the



process of achieving environmental quality.







     More specifically, the primary objectives of the Act



are:






     -Improved practices in land disposal of solid waste to



     protect public health and environmental quality.








     -Regulatory control of hardardous waste from generation



     through disposal.

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                                                         1O






     -Establishment of resource recovery and conservation as




     the preferred solid waste management approach.








     The Act requires or authorizes a number of activities



directed toward achieving these objectives:  Federal regulations



and guidelines; financial and technical assistance to State



and local governments; research, demonstrations, and studies;



and public participation and education.








     The scope of the Federal solid waste program has been



greatly expanded.  This is exemplified in the new definition



of solid waste in the law—not only solids, but also sludges,



liquids, and contained gases are included.   The regulatory



requirements of the law mean that major attention must be



given to waste from industrial and other sources as well as



to municipal refuse, the traditional focus of the solid



waste program.








     I would like to briefly describe the main problem areas



that the program under RCRA is directed to.  Today, over



half our budget and personnel are devoted to working on



hazardous and industrial waste problems.  Industrial waste



generation in the U.S. is estimated at 344 million metric



tons a year with a growth rate of 3 percent a year.  We




estimate there are well over 100,000 surface impoundments



(pits, ponds, and lagoons) where industrial wastes are



placed. We expect that 10-15 percent of industrial waste

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                                                          11
will be classified as hazardous tinder the regulatory program



being developed under RCRA, and that 90 percent of the



hazardous wastes are being disposed of without adequate



measures to protect public health and the environment.  Old



or abandoned hazardous waste disposal sites, as well some in



current use, are causing serious health hazards and destroy-



ing potable ground water supplied.








     Municipal refuse was estimated at around 130 million



metric tons in 1976.  This is about 1,300 pounds per person



per year and is expected to increase to 1,800 pounds per



person by 1985.  About 90 percent of all our municipal waste



ends up in landfills and dumps; about 8 percent is recycled



or processed for energy recovery.  Of an estimated 18,000



landfills, only about 20 percent meet varying State standards,







     The 18,000 municipal wastewater treatment facilities in



the U.S. produce an estimated 5 million tons (dry weight



basis) of sewage sludge each year.  This amount is expected



to double over the next 10 years due to higher levels of



wastewater treatment.  Currently, about 25 percent is spread



on agricultural lands, 15 percent disposed of in the ocean,



and 35 percent incinerated.  We estimate there are 23,000



sludge disposal sites on the land.

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                                                           12
     Among the various environmental problems observed to

result from inadequately managed disposal of waste on land,

degradation of ground water is of greatest concern.  Once

polluted, an aquifer may not be usable as a drinking water

source for decades.  At present about half the U.S. population

is served by ground water.



     Numerous instances of ground water contamination by

leachate from waste disposal sites have been documented.  For

example, of 50 industrial waste sites evaluated in an

EPA study in 1977, 43 showed migration of hazardous constituents

into ground water.
                           '•)


     In addition to ground water contamination, improper

disposal practices have led to direct exposure of humans to

toxic wastes, contamination of surface waters by runoff from

disposal sites, air pollution, damage to wet lands and other

environmentally sensitive areas, explosions of landfill gas,

contamination of croplands with heavy metals, and other

effects.



     Resource recovery systems can alleviate our land disposal

problems while contributing to our resource supplies.  A

number of interrelated factors have held back more rapid

expansion of resource recovery in this country, however:

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                                                           13






Land disposal has been relatively cheap, at least in terms



of direct costs—environmental damage has been largely



ignored and, compared with many other countries, land has



been plentiful.  Most communities lack the experience, expertise,



and organization required to plan effectively for resource



recovery.  There are technological uncertainties.  Markets for



recovered materials have been limited and highly unstable.



National policies have encouraged use of virgin resources.



Until recently, fossil fuels have been plentiful and cheap,



dampening interest in wastes as fuels.







     As land disposal becomes more difficult and resources more



costly, however, many U.S. communities are now seriously



cnsidering resource recovery systems.







     Under the Resource Conservation and Recovery Act, the



following course of action is being taken in response to



these problems.







     Each of the States, with financial and technical assistance



from EPA, is to develop comprehensive solid waste management



plans.  There are two major aspects of the plans.  One is the



evaluation of all land disposal sites against environmental



criteria.  Sites not meeting the criteria are to be closed




or upgraded.  The second major task is for each State to




develop and implement a hazardous waste regulatory program

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                                                              14
controlling hazardous wastes from the point of generation


through final disposal.  In those States that do not implement


an EPA-authorized hazardous waste regulatory program, EPA


will administer the program.  In 1979, Federal financial


assistance to States for development of their solid waste


programs will total about $30 million.




     EPA minimum criteria for solid waste disposal facilities,


which are now being developed, will define environmentally


acceptable disposal.  States can elect to have higher


standards.




     Because of the broad definitions of "solid waste" and


"disposal" in RCRA, the criteria will apply to almost all


wastes and all forms of disposal on land, including dumps,


landfills, land-spreading of sludge, and surface impoundments


(pits, ponds, lagoons).




     Main concerns are:



     "Protection of the quality of ground water, surface


      water, and the air.



     "Protection of environmentally sensitive areas, such a


      wetlands.


     °Prevention of adverse health effects from spreading


      sludge on land used for food-chain crops.

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                                                          15





     °Prevention of safety hazards and breeding of disease



      vectors.







     The evaluations of disposal sites against the criteria



must be thorough since they may serve as the basis for



enforcement actions.  The total inventory process is expected



to take several years.






     Open dumps are to be closed or upgraded within a



reasonable time after the inventory (not to exceed 5 years)



in accordance with State-established compliance schedules.



States must implement this program to eliminate open dumps



in order to continue eligibility for Federal financial aid



for their solid waste management programs.








     The key provisions in RCRA for the hazardous waste



regulatory program are directed to development of criteria



for identifying hazardous wastes, institution of a manifest



system to track wastes from generation to disposal,



and establishment of a permit system for hazardous waste



treatment, storage, and disposal facilities.  Seven sets



of regulations for this program are now under development.



Most of them have been formally proposed; they are



scheduled to be issued in final form by the end of the



year.  Under the proposed regulations, wastes will be considered



hazardous if they are toxic, corrosive, reactive, or ignitable,



as determined by standard identification methods, or if they



apprear on a list of approximately 160 wastes included in



the regulations.

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                                                              16




     Waste generators will be responsible for determining



whether their wastes are hazardous.  EPA estimates there are



approximately 270,000 hazardous waste generators, The industries



heavily represented would include organic chemicals, primary



metals, electroplating, inorganix chemicals, textiles,



and petroleum refining.








     The proposed standards for hazardous waste treatment, storage,



and disposal facilities include design and engineering standards



to contain, neutralize, or destroy the wastes so they cannot



contaminate ground water, surface water, or the



air, and management requirements such as safety and emergency



measures, training of personnel, and recordkeeping and



reporting.  These proposed standards also require financial



responsibility for each site amounting to $5 million per damage



incident during site operation and the setting aside of funds



sufficient for properly closing the site and monitoring and



maintaining it for 20 years after closure.  EPA estimates



that approximately 30,000 permits will be issued by EPA and



the States under the regulatory program to those who store,



treat, or dispose of hazardous wastes.








     A major problem in the United States is finding acceptable



sites for hazardous waste facilities, municipal landfills, and




other waste management facilities.  In some instances, we have



even had a difficult time in locating sites for resource recovery



facilities.  Sites determined to be acceptable from environmental



and economic viewpoints are frequently made unavailable due to



public opposition.

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                                                         17






     One recent study has attempted to describe what cities



are doing in the face of such opposition.  Where there are



large amounts of land suitable for disposal purposes within



a relatively short distance, cities normally just kept looking



until a non-controversial site could be acquired (usually



in a remote area).  In situations where appropriate land



was in short supply and expensive, resource recovery was proposed



and is being implemented.  This is particularly applicable to



large cities, especially in the Mid-Atlantic and New England



states.  Only a few cities took the necessary steps through



condemnation and court action to use the preferred disposal



site.








     We have begun a public education program with the siting
                                   Ti


issues as an area of emphasis, and we are exploring the



various approaches that might be taken to ease the situation,



but it seems clear that siting will loom as an obstacle for



some time to come.







     The siting problem is a major impetus to municipal



resource recovery.  By 1985, it is projected that 10-15



percent of municipal solid waste in this country may be processed



for energy recovery.  Wastepaper collection and other



recycling programs are also on the increase at present,



particularly in the northeast and California.

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                                                              18





     To encourage resource recovery and conservation, RCRA




requires or authorizes a number of EPA activities, including




technical and financial assistance to State and local governments,




guidelines, analysis of Federal policies affecting resource



conservation, and research, development, and demonstrations.








     Inadequate planning and consultation 'has been a major



barrier to more rapid implementation of resource recovery



systems.  To help cities overcome this problem, we recently



established a program of financial assistance to communities



in the planning and development of resource recovery projects.



In February 1979, 68 communities were selected to receive such



aid totaling $15 million.








     Technical assistance in resource recovery takes several



forms: The EPA Regional Offices make available specialists to



assist State and local governments; we present seminars



around the country on how to implement resource recovery



systems; and assistance is provided in setting up "waste



exchanges," which are clearinghouses for promoting the



transfer and utilization of industrial waste materials.



Twenty or more such exchanges have been established around



the nation.

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     Three guidelines that include mandatory provisions for



Federal agencies are being monitored:  The Guidelines for



Source Separation have led to the participation of 175,000



Federal employees in paper recycling programs.  Under the



Guidelines for Beverage Containers, 13 of 51 reporting



agencies are requiring, on an agencywide basis, the placing




of refundable 5-cent deposits on all beer and soft-drink



containers sold in their facilities.  Under the Resource



Recovery Facilities Guidelines, thus far Defense Department



installations in nine metropolitan areas are planning to



operate or utilize resource recovery plants.








     Section 6002 of RCRA requires that procurement with



Federal funds be items composed of the highest percentage



of recovered materials practicable.  EPA is developing guidelines



for recommended procurement practices.  The first guidelines



will be on use of fly ash and blast furnace slag in making



cement and concrete.








     RCRA established the interagency Resource Conservation



Committee to study present and proposed Federal policies



related to resource conservation.  The Committee has issued



reports on beverage container deposits and on the concept of



the solid waste disposal charge -- a tax on products that



contribute to the municipal solid waste stream.  The final



report and recommendations of the the Committee are now in



preparation.

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                                                         20
     Several types of activity were carried on to develop



information and technology regarding resource recovery:




technical, economic, and environmental assessments of



commercial-scale resource recovery facilities; demonstrations



of resource recovery systems; research projects in recovery



technology; case studies of three municipally sponsored




source separation programs; and a national survey of programs



for separate collection of wastepaper and other recyclables.








     In all our major activites we are encouraging public



involvement.  RCRA requires EPA and the States to provide



for public participation in the development of all regulations



and programs.  We have held about 150 public meetings across the




country to explain and obtain comments on the major issues.



The information and views thus elicited are adding greatly



to the quality of our regulations and policies.  We also have



public education activites to inform the public about RCRA



and to help them participate effectively and constructively.








     That, in brief, is the present Federal program in solid



waste management.  Because of the large scope of the program



and the costs involved, we expect this to be long-term effort.



It will be many years before we can say we have the environmental



problems associated with solid waste disposal under control



and have reached our potentials in resource recovery.  We can



claim, however, that today at last we have a program clearly



directed toward those essential goals.

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                                                                          21
          Status of the Solid Waste Effort in the U.S.
           Discussion Leader:  Mr. John W. Thompson

Question:  In Japan, the role of each generator, enterpriser, undertaker

           of  solid wastes, municipality, prefectural government, National

           Government,  etc. on solid waste management is prescribed by

           the  'Waste Disposal and Public Cleansing Law'.  How is it in

           the U.S.?  And what do you think about this matter?

Answer:    We in the United States have never prescribed anything for our

           ordinary municipal waste.  We have no national law and no
           control over the generator and the hauler of municipal waste.

           But, with the new legislation we will have control over the
           landfilling of it.
Question:  Maybe we should ask the question in another way.   What we would
           like to know is whether each municipality has the responsibility
           of managing its own domestic waste?
Answer:    Yes, each municipality has the responsibility for managing its
           own domestic waste.  Generally, the communities do this through
           ordinances.
Question:  What about industrial wastes?
Answer:   With our new legislation, we are setting up a manifest  system to
          cover the generator, hauler and disposer of hazardous wastes.
          The state of California now has one of the best manifest systems

          and we would like to see similar systems adopted throughout the
          United States.   It is a three-part form.  The generator fills

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                                                                            22
           out the first third and sends it to the state; then the hauler




           fills out a second portion and sends it to the state; and




           the final disposer also fills out the form.  Eventually they




           should all come  together at the state level.  We then




           have the capability of following hazardous waste through-




           out the system.




Question:  In the United States, how could you estimate total amount of




           solid waste discharged now and in the future?  In Japan, the




           total amount of domestic solid wastes discharged is estimated




           by summing up municipalities' actual data.  For industrial wastes,




           solid waste generation is estimated on tonnage of production or




           per units sold.




Answer:   We do not collect statistics for every city.  However, we have




           conducted several studies that examined a representative sample




           of cities. We have then taken this representative sample, and




           by applying statistical means, have calculated national figures




           for solid waste.  There are a few things we know about genera-



           tion of solid waste pel* person.  It varies by income.  Poor




           people do not generate the most solid waste.  We know that




           for every one percent increase in income, solid waste gen-




           eration increases 0.75 percent.  It is very difficult for




           us to develop national figures OR solid waste because some




           solid waste is compacted, some is noncompacted; some is




           weighed on scales while some is estimated by cubic yards




           on the truck.  We estimate our industrial waste in a

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                                                                         23
           similar manner to that of the Japanese.   That is,  we estimate




           industrial waste based on production.   And this estimate is




           also subject to recessions.  For example, in 1973  and 1974




           when we had a recession in this nation,  the industrial waste




           tonnage was also down.  In other words,  industrial waste moves




           with the gross national product.  We have done 15  special studies




           in hazardous  waste in 15 different industries and  have come




           up with the waste generation for those industries.




Question:  What is the payment system for solid waste management in the




           United States?  We would like to know about fee and/or  general




           tax.  How are municipalities and private industries involved




           for collection and disposal of domestic  solid wastes?  How




           about industrial waste?  The charge system in Japan is as




           follows:  In almost every municipality,  collection and dis-




           posal of domestic solid wastes is free of charge.   However,




           for bulky refuse (for example, TVs, refrigerators, sofas,



           etc.) a fee is charged to the disposer by the amount discharged




           or by a fixed charge in many municipalities.   Other aspects




           in this matter are described in "Solid Waste Management in



           Japan."




Answer:    Sixty-five percent of our wastes are collected by  the cities




           out of general tax revenues.  The remainder is collected by




           private haulers who usually charge each  customer.   A few




           cities pay the private hauler from general tax revenue funds.




           On the bulky waste,  some cities collect  once a week, once a




           month,  or maybe only twice a year.  In other cities a citizen

-------
                                                                     24
           must call a private hauler to come  to  the house.   He  probably




           will charge about $10.00 to pick  up the  refrigerator  or  stove.



           A few of our cities (maybe 3%)  have user charges  based on  the



           size or weight of the item.  User charges per  item in the




           United States have little, if any,  effect on waste generation



           and in most cases they are difficult to  manage.



Question:  We Japanese  hear that there is a "Solid Waste Information



           System" in the United States.   We would  like to know  about the



           system and whether we could use it  or  not.



Answer:    Yes we have one;  but we are getting ready to discontinue it



           or give it to somebody.  It's called SWIRS — Solid Waste



           Information Retrieval System.   We punch  in key words  and we



           receive a computer printout with  a  short descriptive  paragraph,



           But, our cost, based on the number  of  users, is very  high  and



           we are discontinuing the system.

-------
1.   Status Report
             1-1   So3,id Waste  Management in Japan
                   Ministry of Health and Welfare

-------
                                                                    26

                              CONTENTS


                                                                Page

1.  General 	    1


2.  Domestic Wastes 	    2

  2-1  Present Status of Domestic Wastes Treatment 	    2

  2-2  Strategies for Management of Domestic Wastes 	    3

  2-3  Investigations and Researches on Domestic Wastes 	:    6

    2-3-1  Investigations and Researches Conducted
           in Fiscal 1977 	    6

      (1)  Investigation of Wastes Recycling in Japan 	    6

      (2)  Development of Urban-Environment Planning Methods
           Toward Built-in Recycling 	    7

      (3)  Investigative Research and development on the
           treatment of Ash and Dust discharged from
           Refuse Incineration Plants 	    7

      (4)  Investigative Research on Wastes Hardly Disposable
           Adequately 	:	,	    8

      (5)  Miscellaneous 	    8


3.   Industrial Wastes 	    9

  3-1  Current Aspects of Treatment of Industiral Wastes 	    9

  3-2  Countermeasures to Industiral Wastes 	   14

    3-2-1  Survey Relating to Industrial Wastes 	   14

    3-2-2  Basic Plan for Regional Disposal of Industrial
           Wastes 	   14

  3-3  Investigations and Researches on Industrial Wastes  ....   15

    3-3-1  "Study on Formulation of Master Model for
           Treatment of Hazardous Industrial Wastes" 	   15

    3-3-2  "Study on Formulation of an Emergency Inspection
           Manual of the Industrial Waste Treatment Facilities"   16

-------
                                                                         27
    3-3-3  "Study on Application of Metal Refining Technology.    16






4.  Future Strategies of Waste Treatment 	    16




  4-1  Treatment of Domestic Wastes 	    16




  4-2  Treatment of Industrial Wastes  	    18




  4-3  Securing the Regional Wastes Disposal  Sites 	    18
                                   -  11  -

-------
                                                                      28
1.  General





         In 1970, the Public Cleansing Law was amended entirely and




    substituted by the Waste Disposal and Public Cleansing Law




    (hereinafter, to be referred to as "Waste Disposal Law")  enacted




    for the purpose of conserving the living environment and improving




    the public health.  Under the law, the wastes were classified into




    two kinds.  One is the industrial wastes discharged in connection




    with the business activities.  They are hardly disposable on




    account of the quality as well as quantity so that the responsi-




    bility of disposal is placed on the enterprises concerned.   The




    other is the domestic wastes mainly from households,  and the




    disposal is the responsibity of the respective municipalities.




         However, upon elaspe of eight years since the enforcement




    of the law, wastes management is increasing its importance.   At




    present, it has the following as important problems to be resolved




    urgently:






    (1)   That, with improvement  of the living standard of the people,




         there is an increasing  proportion of the wastes that are




         hardly disposable in the municipal cleansing  scheme such as,




         for example,  scrap home electric  appliances,  construction




         waste materials and plastics;






    (2)   That, against increasing necessity for acceleration of  the




         provision of wastes treatment facilities,  the area in which




         it is difficult to install such a facility because the




         difficulty of obtaining the consensus of the  inhabitants is

-------
                                                                    29
         spreading not any in urban areas but in rural areas;







     (3)  That, while the responsibility for disposal of industrial




         wastes has been defined clearly through amendment of the




         Waste Disposal Law in 1976, there is generated a field where




         it is required for the public organizations to participate




         in the disposal of industrial wastes; and







     (4)  That while there have been developed a number of new treatment




         techniques recently, it has become a problem what choice




         should be made of them for the cleansing project conforming




         to the circumstances of the area concerned.




         For these problems, the government is going to take measures




         upon a long ranging vision, and they are taken as important




         measures with national budget increased at a rate of 30




         percent or more every year recently.  The government will




         also exercise financial as well as technical guidance and




         support for furtherance of the administration of wastes




         disposal in the future.









2.  Domestic Wastes





  2-1  Present Status of Domestic Wastes Treatment





            As regards the "domestic wastes"  produced mainly from the




       daily living activities of the people  such as night soil and




       refuse, the municipalities determine the  disposal  programs




       from collection to final disposal and  dispose of them as one




       of the services to the inhabitants  respectively.
                                - 2 -

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                                                                  30
          Treatment of the refust among the domestic wastes is




          shown in Table 1.  First, the refuse is incinerated, as




          a rule, for the purpose of reducing the volume and stabiliz-




          ing, then disposed the residue as reclamation.  As of the




          end of fiscal 1976, the refuse treated by incineration




          constituted about 68.1 percent of the total amount of




          gathering.  In the refuse treatment, it is required to




          exercise every precaution for processing of emission




          gases and drainage so that air,  water and other environ-




          mental pollutions will be prevented.




               In Table 2 are shown the forms of schemes of collect-




          ing the refuse.  As seen, they vary from city to city or




          town to town due to differences  in the historical and




          social backgrounds of the respective cities or towns.







2-2  Strategies for Management of Domestic Wastes





          At the beginning of fiscal 1977, the refuse incineration




     plants had the capacity increased by  10.4 percent over fiscal 1976.




     The number of the facilities for treatment of bulky refuse at




     the beginning of fiscal 1977 is 252.   The high speed composting




     facilities number  14 with a treatment capacity of 564 tons/day.




     The sites of disposal by reclamation  are shown in Table 4.

-------
                                                                                                                                      31
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-------
                                                              32
    Table 2  Status of refuse collection (whole country)

Government ( Direct management
(City, Town, <
Village) ( Contract
By approved contractors
Total
Refuse collection
54,077
17,693
5,893
t/day

77,663
Table 3  Status of refuse incineration plant construction
         (on the basis of initiation of the construction
         work — whole country)
Fiscal year

1965
1970
1973
1974
1975
1976
Number of plants

1,409
1,293
1,637
1,665
1,718
1,736
Treatment capacity
t/day
20,736
53,998
105,633
111,228
114,559
126,417
            Table 4  Disposal by reclamation

Fiscal
year

1975
1976
Number of disposal
by reclamation

Moun-
tainous
site
1,477
1,616

Sea

41
34

Lake or
River

77
87

Flat
land

847
942

Total

2,442
2,679

Total
area
(1000m2)

65,493
51,427

Total
volume
(1000m3)

344,117
378,081

Remaining
volume
(1000m3)

192,946
244,623

-------
          As regards the financial measures of the government concern-




     ing development of the domestic waste treatment facilities in




     fiscal 1978, there were appropriated as subsidies to the munici-




     palities ¥12,000,000,000 for night soil treatment plants,




     ¥28,300,000,000 for refuse treatment plants, ¥2,900,000,000 for




     final disposal facilities, ¥3,500,000,000 for drainage and




     emission gas processing facilities on refuse treatment plants




     and ¥500,000,000 for the other facilities and also ¥1,100,000,000




     for the projects of the other ministries and agencies concerning




     wastes management, or total ¥48,300,000,000 in an increase of




     39.5 percent over fiscal 1977.




          Further, subsidies in an amount of ¥338,250,000 in total




     are appropriated for the experimental project of pneumatic




     conveying system for collecting and transporting of refuse and




     for the wastes recovery project named "Urban and Rural Environ-




     mental Combination System (URECS)" intended for agricultural




     use of the compost and thermal energy produced by composting and




     incineration of refuse and night soil.






2-3  Investigations and Researches on Domestic Wastes





  2-3-1  Investigations and Researches Conducted in Fiscal 1977





         (1)   Investigation of Wastes Recycling in Japan





                   In these years,  many municipalities  are endeavoring,




              in order to reduce the generation of wastes or save




              the resources or energy,  for sponsoring disused arti-




              cles exchange bargains or making collective recovery

-------
                                                        34
     of wastepaper,  empty bottles,  iron scrap,  etc.  or,  for

     wastes recycling,  utilization of the heat  generated

     from the incinerator for hot water supply  or power

     generation.   Under the present survey,  it  was intended

     to grasp the actual condition of the wastes recycling

     conducted by the cities and all intermunicipal  public

     agency including cities throughout the  country,  and

     there were obtained useful data for promotion of the

     wastes recycling in the future.


(2)   Development of  Urban-Environment Planning  Methods
     Toward Built-in Recycling


          This research was carried out for  three years

     successiviely from fiscal 1975, and in  1977 it was

     summed up as the final year of the research.  That  is,

     administrative  procedures were examined for establish-

     ment of a waste recycling system designed  not only  for

     an individual city,  town or village but for regional

     area including  cities,  towns and villages  or a macro

     urban area,  and a  specific program was  proposed.


(3)   Investigative Research and development  on  the Treatment
     of Ash and Dust discharged from Refuse  Incineration
     Plants


     This research and  development  is intended  to  develop

     a  technology for reuse of the  burnt ash and precipitated

     dust in order to reduce the final  amount of disposal

     and also a technology  for prevention of effluent  of
                     - 7 -

-------
                                                        35
     hazardous materials against the burnt ash and preci-

     pitated dust that may contain hazardous materials.   In

     fiscal 1977, a survey of the actual condition was

     conducted, and there were obtained basic data for

     future study.


(4)   Investigative Research on Wastes Hardly Disposable
     Adequately


          Under this research,  a survey of the actual

     condition was made of the wastes preculding  adequate

     treatment in the current urban cleansing system, and

     the causes and reasons of the difficulty of  adequate

     treatment were clarified,  with basic data obtained  for

     resolution of the problems surrounding the wastes

     precluding adequate treatment.


(5)   Miscellaneous


          As the other researches in fiscal 1977,  there

     were conducted the "formulation of quidelines for

     treatment of refuse in the sightseeing sites", the

     improvement of compost system and agricultural aspects

     on  municipal solid wastes" and  "development  of leacheate

     treatment system at the disposal  site" with  basic data

     obtained for future studies respectively.

-------
                                                                    36
3.  Industrial Wastes





  3-1  Current Aspects of Treatment of Industiral Wastes





            The industrial wastes  comprise  as many  as  19  kinds  of




       wastes including cinders, sludge,  etc. and,  by  summing up the




       surveys conducted independently by prefectures,  their total




       amount of discharge is  estimated to  be about 320,000,000 tons




       a year (Table 5}.  For  treatment of  such a enormous amount of




       industrial wastes,  provision and improvement of treatment




       systems are being advanced,  and serving as a basis of the




       regional treatment system,  there is  a treatment program  deter-




       mined by the prefectural governor.   Under such  program,  it is




       intended to establish an adequate  treatment  system pursuant to




       the characteristics of  the  respective prefectures.  As of




       December 1978,  such programs have  been formulated  in 45  pre-




       fectures .
                                - 9 -

-------
                                                                  37
                Table 5  Discharges of Industrial Wastes
                         throughout the Country (Annually)
Kind of industrial waste
Cinders and dust
Sludge
Waste oil
Waste acids and alkalis
Waste plastics and rubber scrap
Waste paper, wood chips and rags
Vegetable and animal remnants
Livestock excretions and corpses
Metal scraps
Glass and porcelain chips
Slags
Construction waste mateirlas
Total
Annual discharge
(10,000 tons/year)
930
5,330
340
5,240
160
1,820
660
4,220
810
220
4,440
7,830
32,000
Discharge
percentage
2.9
16.6
1.1
16.4
0.5
5.7
2.1
13.2
2.5
0.7
13.9
24.4
100.0
(Note)  1.   Simple total of the  discharges  investigated by the prefec-

           tures  over the  years of  1970  to 1974, and the years of

           investigation are  not always  the same.


       2.   The  foregoing classification  of the wastes is not a standard

           one.   For  example, some  prefectures included sand in the

           construction waste materials.


       3.   The  discharges  surveyed  by  the  prefectures included those

           of actual  survey as  well as estimates from the original units.
                                - 10 -

-------
                                    J8
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-------
Table 7  Industrial Waste Treatment Facilities
         (as of 1 May 1978)
                                                          39
Kind of
facility
Sludge dehydration facility
Sludge drying facility
Sludge incineration facility
Waste oil oil"water separation
facility
Waste oil incineration facility
Waste acid or alkali neutrali-
zation facility
Waste plastics crushing
facility
Waste plastics incineration
facility
Concrete solidifying facility
Mercuric sludge roasting

facility
Cyanide decomposition facility
Sub-total
Disposal sites for hazardous
wastes
Disposal sites for waste
plastics and rubber scrap etc.
(Leacheate treatment facilities
are needless)
Disposal sites for sludge etc.
(Leacheate treatment facilities
are need)
Sub- total
Total
Total
number
2,760
178
413
499
361
623
87
786
95



346
6,153
25


170


599

794
6,947
Installator
Enterpriser
2,515
131
374
393
252
605
39
623
55



333
5,323
16


83


312

411
5,743
Contractor
75
15
25
102
108
16
47
154
39



11
594
9


85


276

370
964
Public
body
170
32
14
4
1
2
1
9
1



2
236
o


2


11

13
249
                     - 12 -

-------
                                                                40
     Treatment of the industrial wastes includes that per-




formed by the enterprisers themselves, that by the contractors,




that performed over a regional area by the prefectures and that




performed jointly with the general wastes by the cities, towns




and villages respectively.  The cases of licence granted to




the contractors for treatment of industrial wastes as of May




1978 are as shown in Table 6, and the facilities for treatment




of industrial wastes as of May 1978 are shown by the installing




entity in Table 7.  The total number of installation of process-




ing facilities is 6,153, indicating a steady increase over 4,849




in February 1976 and 5,343 in May 1977 and thus improvement in




the treatment system.  The total number of final disposal sites




is 794.




     Treatment of the industrial wastes is originally the




responsibility of the enterprisers under the Waste Disposal




Law, but it is allowed for the city, town, village or prefec-




ture to perform the treatment of industrial wastes as its task.




     Nowadays, however, difficult problems are occurring in the




treatment of industrial wastes by the enterprisers themselves




or the contractors, and there are increasing cases of the local




public organizations performing the treatment of industrial




wastes directly or indirectly from the point of view of conserv-




ing the regional environment, and as of May 1978, the industrial




waste disposal by public participation is carried out at 14




prefectures and 10 cities.
                          - 13 -

-------
                                                                 41
          In view of such situation, the Ministry of Health and




     Welfare is examining specifically what should be the partici-




     pation of the public in the treatment of industrial wastes.







3-2  Countermeasures to Industrial Wastes





  3-2-1  Survey Relating to Industrial Wastes





              For the purpose of obtaining the fundamental data for




         adequate execution of the industrial waste disposal/  the




         Ministry of Health and Welfare conducted a survey of  the




         discharge of industrial wastes in fiscal 1977.   In this




         survey, the kinds and quantities of industrial  wastes




         discharged from various enterprises were investigated in




         a countrywide scale to grasp the actual condition.







  3-2-2  Basic Plan for Regional Disposal of Industrial  Wastes





              The problems concerned with the industrial wastes are




         becoming increasingly complex and difficult year after year.




         For example,  the difficulty of obtaining the land for final




         disposal of industrial wastes is impending.   Here,  in pre-




         paration of a regional disposal system covering the whole




         area of a prefecture,  the Ministry of Health and Welfare




         selected 4 representative prefectures by type of the  dis-




         posal and presented the basic plans formulated  in these




         prefectures as  models  to the entire prefectures in  fiscal




         1977.   This representation is intended for  the  respective




         prefectures to  carry out a wide area disposal adequately




         in  accordance with  their respective actual  conditions.









                               - 14 -

-------
                                                                      42
3-3  Investigations and Researches on Industrial Wastes


          The Ministry of Health and Welfare is conducting inves-

     tigations and researches on the treatment of industrial wastes

     every year.   In fiscal 1977, the following three investigative

     researches were carried out for furtherance of the adequate

     treatment of industrial wastes upon the findings of the inves-

     tigations and researches so far conducted concerning the

     treatment of industrial wastes and for formulation of more

     specific and practical guidelines.
  3-3-1  "Study on Formulation of Master Model for Treatment
         of Hazardous Industrial Wastes"
              By the surveys conducted in fiscal 1975  and 1976

         throughout the country of the hazardous industrial wastes

         the countrywide status of the discharge,  treatment and

         recycling of the hazardous industrial wastes  was disclosed.

         But,  for further promotion of the adequate treatment of

         hazardous industrial wastes,  there are required countrywide

         and long ranging measures including provision of social

         systems concerning wastes recycling.  Thus,  in order to

         execute the foregoing at public level as  well as private

         level with the target placed  on a national level, patterned

         master models'were presented, while a process of decision

         making for choice of an adaptive model was developed.
                               - 15 -

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                                                                43
    3-3-2  "Study on Formulation of an Emergency Inspection Manual
           of the Industrial Waste Treatment Facilities"


                In view of a number of cases of inadequate treatments

           of industrial wastes, it is required for the enterprisers

           themselves to inspect their own industrial waste treatment

           facilities and correct any improper places and also for the

           prefectures as well as cities specified by the ordinance to

           exercise pertinent inspection and guidance.  For such

           purpose,  there was formulated a guideline for design and

           inspection that would serve as standards for installation

           and operation of the treatment facilities.


    3-3-3  "Study on Application of Metal Refining Technology
           to Hazardous Sludge Treatment"


                Studying the cases of applying the technology of re-

           covering the heavy metals in the sludge as metallic resources

           practically in use of the available metal refining technology,

           the possibility of expanding the application in the future

           was elucidited.



4.  Future Strategies of Waste Treatment


  4-1  Treatment of Domestic Wastes


            For the refuse  treatment, the treatment system is formed

       presently around the method of making an incineration treatment

       which is capable of  reducing the volume of refuse to the

       minimum among other  treatments and using the burnt ash for

       landfill.
                                 - 16 -

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                                                                44
     For recycling of the refuse, on the other hand, it is




required mainly from the point of view of reducing the volume




of refuse to examine the specific measures positively in the




processes of generation and treatment of refuse.  But, generally




in Japan, wastes recovery is not satisfactory in the aspect of




technology as well as system so that what is expectable for




the time being is to tackle the problem of wastes recovery




pursuant to the actual condition of the respective areas.




     For improvement of the refuse treatment facilities which




play a main role for smooth execution and promotion of the




refuse treatment project, it is being carried out systematically




in accordance with "Fourth Five Year National Program for Waste




Treatment and Disposal":  But, in some areas, it is becoming




difficult to secure sites on account of higher density in land




use on one hand and increasing requirement for environmental




conservation measures on the other.  With difficulties thus




produced in the improvement of the facilities, it is requried




in such areas to cope with the situation by, for example,




planning a regional refuse treatment and exerting efforts for




improvement of the equipment relating to prevention of pollutions.




     Further, for the pneumatic conveying system and the wastes




recovery project named "URF.CS" that are being carried out as




experimental projects, it is required to assess them technically




as well as economically in consideration of the social back-




grounds of the experimental areas and then examine the possibility




of generalization of the experimental projects.
                          - 17  -

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                                                                   45
4-2  Treatment of Industrial Wastes





          With enforcement effective 15 March 1977 of the law




     enacted at the 77th ordinary session of the National Diet for




     partial amendment of the Waste Disposal Law, a legal system




     was provided which clearly set forth where the responsibility




     would lie in the processes of from discharge to final disposal




     of the industrial wastes.  The industrial waste treatment




     system is, of course, framed upon the principle of the enter-




     prisers being responsible for the treatment.  But, nowadays,




     there are generating cases where it is difficult for the




     enterprisers to execute the responsibility by their own efforts




     only.  Thus, there are increasing cases where the local govern-




     ment establish a corporation, etc. and participate directly in




     the treatment.   In the Ministry of Health and Welfare, it is




     contemplated to collect information concerning the generation




     and flow of industrial wastes, exert efforts particularly for




     research and development and also assessment of the industrial




     waste treatment techniques and carry out education and training




     and thus positively lay the foundation for the treatment of




     industrial wastes to be made adequately.






4-3  Securing the Regional Wastes Disposal Sites





          Discharge  of the wastes is expected to increase hereafter,




     and efforts may be made for promotion of the recovery of wastes




     or developemnt  of processing techniques, yet there will be  a




     considerable amount of wastes requiring final disposal.   On the
                               - 18 -

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                                                            46
other hand, it has become increasingly difficult in these




years to find the final disposal sites which are indispensable




for adequate treatment of the wastes, and there arise problems




which are hardly resolved by the self-supporting efforts of




the cities, towns and villages or enterprisers alone.  Parti-




cularly, in the greater urban areas such as metropolitan area




and Kinki area, establishment of the final disposal sites is




extremely difficult in that the land is used in higher density.




     It is thus contemplated to encourage the pertinent regional




disposal systems such as joint treatment by some inter-municipal




public agency or enterprisers or participation of the prefectures.




Further, in the metropolitan area and Kinki area where it is




considered there is a necessity produced for integral regional




final disposal program, it has been determined to study the




measure of constructing the regional waste disposal sites at




the government level for use by municipalities, and a pre-




liminary survey has been carried out since fiscal 1978, and




the regional waste disposal systems in the metropolitan and




Kinki areas will be improved upon the result of the survey.
                          - 19 -

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                                                                47
                     Solid Waste Management in Japan
              Discussion Leader:  Mr. Tadayuki Morishita

Question:  Table #1 indicated that there has been a 10 percent decrease
           in waste generation per person per day since 1972.  Why?

Answer:    The higher figure for 1972 than, for example for 1974, can
           be explained by the fact  that in 1972 we collected the waste
           from domestic sources and from industrial sources giving
           a larger combined total.  Today, we are making the industrial
           generators responsible for taking care of their own industrial
           waste. Actually, what we are talking about when we say "indus-
           trial waste" is commercial waste—from commercial sources like
           department stores.  These wastes are very similar in kind to
           those from domestic sources.   Those decreases that you point
           out, for example in 1973 and 1974,  from the 1972 figures can be
           explained by the fact that some of the recycling processes
           had begun,  especially the recycling of paper waste.   We might
           be able to find another reason for this decrease as well.  In
           Japan, as well as in the United States, as Mr.  Thompson
           has explained, there have been some differences in measuring
           waste—some by volume, some by weight.  These figures reflect
           the sum of all of these municipal statistics.   So, over these
           several years there has been an improvement in collecting
           data.  For example, we are now using trucks which can hold
           two tons.   However, even if the trucks have a one-ton load,
           we count it as two tons.  So,  this  practice might make some

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                                                                         48
           difference in measuring solid waste generation.




Question:  Table #4 indicates that some solid waste ends up in the sea,




           river or lake.  In what form is the waste placed in these




           areas and what safeguards against water pollution do you take?




Answer:    Although I do not have the technical documents with me that




           relate to the scientific answer to that question, I can




           explain one example of sea disposal.  First of all, we rely




           on a series of dikes composed of clay, gravel, and soil.  Dikes




           measure 50 to 80 meters on the bottom and IS meters high.




           And of course we use an impervious material inside   the dike.




           In Tokyo, we have an off-shore site.  In this case, the




           cost is $100,000 for the dike.  The expense in terms of




           volume of waste is $27.00 per cubic meter of waste.  (If




           there is 1,000 kg per cubic meter, the specific gravity




           will be one.)




Question:  I assume these are dry dikes and they are built off-shore?




Answer:    First we set up an off-shore dumping site by surrounding the




           site with a dike.  Then we pump out the water leaving about




           three meters in the bottom.  The waste is then dumped in




           losse and compacted.




Comment:   That is very interesting.  As a matter of reference, in the




           United States, we do not allow ocean dumping of solid waste




           in the ocean at all.  It is prohibited by law—except for




           sewage sludge.  And sewage sludge will be phased out by




           1981.  Also, we do not allow sewage in navigable

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                                                                          49
          waters, e.g., rivers on lakes.
Question: Initially I had a question about the flotation of the light
          material and its spilling over into the ocean; but it is
           apparently not that wet?
Answer:   That is correct.  When we start to dump some waste into
          the dike, we also bale out water at the same time.  We
          process this water so it is pure before it is discharged.

Question: A miscellaneous research project in fiscal 1977 was the
          development of a leachate treatment system at the disposal
          site.
Answer:  I would like to skip this question because this afternoon Dr.
         Yagome is going to present his paper on leachate treatment and
         we undoubtedly will have a substantial discussion on the
         subject at this time.

Question:Table #7 indicates that there are 25 disposal sites for hazardous
         wastes.  Please describe the sites and what is done to avoid ground
         water contamination?  Also, there are 794 final disposal sites
         for industrial wastes.  What control and safeguards do you have
         over these sites?
Answer:  I would like to respond tothese questions at the same time.
         The wastes from glass and plastics are very stable.  Consequent-
         ly, we do not have very strict regulations on disposal of these
         wastes.   However, in the case of decomposable waste—like
         garbage— we have some regulations requiring leachate treatment
         before disposal.   .As for hazardous wastes,  we have regulations

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                                                                        50
           requiring  storage in concrete tanks or some other safe


           disposal method so that these wastes never mix with ground


           water.  Implementation of hazardous waste treatment requires


           that the disposer receives approval from the municipality


           before he can construct the treatment facility.  The allowable

                                                -7
           standards of permeability would be 10   per centimeter per


           second.


Question:  We like the idea of regional disposal of solid wastes.  Please


           explain the models you are developing on regionalization and


           what you are doing to acquire land for the facilities.


Answer:    In Japan we have a large-scale power plant called Phoenix.


           I would like to explain the reason we call it Phoenix,  Phoenix


           is a beautiful plant representing the green, sarid and the sea.


           This facility performs reclamation from waste.  The waste


           having becaome useless is first incinerated.  Land is then


           built up by reclamation of the incinerator for residue and


           rises again like the phoenix.  In reality, we have two off-


           shore sites in mind:  one in Osaka and one in Tokyo.  The


           one in Tokyo is 10 square kilometers and the one in Osaka


           is 7 square kilometers.


Question:  You mentioned the regional treatment facilities.  I assume that


           those are for both municipal and industrial waste disposal?


Answer:    Yes, they handle both municipal and industrial waste.  In the


           case of industrial waste, we require them to process  their


           waste first before we let them put the waste into our facility.

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                                                                                51
Question:  Process for what reason?




Answer-:    Tn order to reduce the hazard and reduce the volume.




Question-  You indicated that you had difficulty finding sites for




           disposal too.  Is that related to economics or public resistance.




Answer:    Public resistance.




Question:  You mentioned heavy metals in residual wastes.  What do you do




           about these heavy metals?  Do you have limits?  Tolerances?




Answer:    Yes.  we have some standards for industrial waste  in terms




           of the amount of heavy metals in the waste.  But  to date




           we haue not experienced any excess of heavy metal  in our




           municipal waste.  However, we expect this  to be a  problem




           in the future so that is why we want to develop some




           technology.  If you want the actual standards, they are in




           some of the papers being presented.




Question:  Are these for heavy metals—cadmium, lead, zinc?




Answer:    Yes.




Question:  How will the two facilities that you are planning  be funded?




Answer:    For domestic waste, the Japanese Government is subsidising




           one half of the expense; the other half is coming  from long-




           tsr-m loans.  The industrial waste facility will be financed




           entirely through long-term loans.  We are  thinking about




           collecting that money bach from industrial sources.

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1.   Status Report
           1-2  Current  State of  Pneumatic  Conveying
                Systems  of Domestic Waste
                           1979.  3. 12
                               by
                           AKIO NAMIKI
                Director of Urban Highway Division
                           City Bureau
                     Ministry of Construction

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                              CONTENTS
1.  Perspective of Pneumatic Conveying Systems  of
    Domestic Waste 	
2.   Installation Achievement in Japan
3.  Design Standards of Pneumatic  Conveying Systems of
    Domestic Waste	
                                                                53
                                                                 Page

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                                                              54
          (REPORT ON THE 4TH JAPAN-U.S.  CONFERENCE  ON WASTES)







1.  Perspective of Pneumatic Conveying Systems  of Domestic Waste





         With concentration of  the population in the  large cities,  im-




    provements in living standards,  and  the  advent  of a high  consump-




    tion society, discharge of  waste has increased  drastically  in Japan




    and disposal of this waste  has become a  major governmental  problem.




         Although disposal  of refuse discharged from  each household is




    carried out by the municipalities, with  the ever  increasing volume,




    the work involved in disposal is becoming increasingly more diffi-




    cult.  Problems such as deterioration in efficiency of refuse




    collection with increases in the volume  of  vehicular traffic,




    worsening traffic conditions with increases in  the number of refuse




    collection trucks, and  poor sanitation and  destruction of the




    beauty of the environment with the collection point exists  parti-




    cularly in the city areas as a result of the collection and




    transportation of refuse from the households to the incineration




    or landfill sites.  The need for establishment  of a sanitary and




    functional system of refuse collection is also  heighting  together




    with the construction of high-rise buildings.




         A plan in which pneumatic conveyance is used as the  refuse




    collection and transportation system has been under research and




    study as a means of resolving the foregoing urban environmental




    problems and contributing to the construction of  comfortable




    residential quarters.




         In 1976, a pilot project for the improvement of the  pneumatic




    conveying systems of domestic waste  was  commenced with the  aid  of




    a government subsidy.
                                -  1  -

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                                                                55
2.  Installation Achievements in Japan





         Although pneumatic conveying systems of domestic waste has




    already been installed in individual structures  such as  hotels and




    hospitals in Japan from several years ago and has  been providing




    practical service, a pilot project was launched  in 1976  to resolve




    technical and administrative problems involved in  the installation




    of this system in general city areas and also to confirm the  safety




    of the overall system.   The pilot project was conducted  at both




    the Osaka Nanko Port Town and the Ashiyahama New Town in Ashiya




    city and the general outline of the respective pilot projects is




    as shown in Table 1.  Detailed descriptions  will now be  given in




    relation to Osaka Nanko Port Town with its advanced system.







                               Table 1.
Area Name
1. Project Body
2. Project Details
Area of District
Number of Homes
Population
Overall length
of tubing
Garbage collection
centers
3. Project Period
4. Total project cost
5. Ratio of Government
Subsidy
6. Project Cost from
1976 to 1978
7. Supervisory Body
Nanko Port Town
Osaka City

110 ha
10,136 units
40,500 persons
10,650 m
1 place
Approx. 5 years
from 1976
¥5 billion
1/4
¥2.6 billion
Ministry of
Construction
Ashiyahama New Town
Ashiya City

125 ha
5,700 units
20,000 persons
13,979 m
1 place
Approx. 5 years
from 1976
¥2.9 billion
1/4
¥1.9 billion
Ministry of Health
and Welfare

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                                                             56
     Osaka Nanoko is a vast port city with an overall area of 920




ha which is currently under construction with completion scheduled




for 1980.  Its purpose is to provide port facilities, truck




terminals, residential area, and industrial area and is being




constructed by the Osaka Port Authority by filling in the sea




between the Osaka port area and the Suminoe area.




     Although the nucleus of Osaka Nanko is the port town, it is




also being constructed as a model residential area in a metropoli-




tan city by introducing a new traffic system suitable for a new




city and also introducing new techniques in pneumatic conveyance




of domestic waste.  In addition to construction of houses by the




Japan Housing Corporation, the City of Osaka, and the Osaka Housing




Supply Corporation, schools, parks, and business and commercial




facilities will also be provided.




     Nanko Port Town is composed of 4 residential districts with




an overall area of 110 ha, a population of about 40,000 and about




10,000 houses and construction was launched in July of 1975 with




completion targeted for 1983.  The first housing construction




program of the Japan Housing Corporation has now been completed




and occupation of the 14 story high-rise building has commenced




from November, 1977.  Construction of housing under the second




housing construction program of the Japan Housing Corporation and




the City Housing Corporation is continuing together with construc-




tion of area center buildings, elementary schools and junior high




schools.  A high school has already opened from April of 1977.




     The pneumatic conveying system in Osaka Nanko Port Town will
                             - 3 -

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                                                               57
cover the entire port town area and will collect and transport




waste to the waste collection centers in the port town.  The




collected waste will then be repacked into containers for secondary




transportation and special trucks will carry them to the processing




plant located approximately 4 km away within Osaka Nanko.  Dust




chute type facilities of high-rise buildings shall be employed and




will be installed together with the construction of the houses.




     Operation of this system has now commenced at the Port Town




Administration Center following opening of operations in November




of 1977 in 3 apartment blocks in which occupancy had commenced.




The number of units occupied had attained approximately 1,200 as




of December, 1978 and the, amount of domestic waste discharged is




approximately 1,400 kg/day.




     In July, 1978, a survey was conducted of the users by  means




of a quetionnaire and favorable comments were received from




approximately 90% of those surveyed such as discharge time  is




optional, the system is sanitary, and does not spoil the beauty of




the environment.  The remaining 10% commented to the deffect that




it was inconvenient and bothersome as the refuse post must  be




locked,  the distance of the post is too great, and there is a




limit to the size of refuse it will handle.




     The principal problem points and troubles expected after




commencement of operation and the countermeasures are as follows.







a)   Although there were frequent cases of the dust chute clogging




    at the initial stage due to the unfamiliarity of the users,




    rules for the usage of the refuse posts not closely observed
                             - 4 -

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                                                              58
    etc., this type of trouble was cleared up in approximately 1




    to 2 months after occupancy with thorough guidance given by




    the local council.  (total of 24 cases overall)







b)  Although there were 16 cases where the discharge drum would




    not stop due to malfunctioning of the discharge detector, this




    was overcome by repairing the detector sensor.







c)  There were 4 cases of defective locks on the refuse posts and




    these were overcome by replacing the locks.







d)  At the initial stage of occupancy,  there were 4 cases of drum




    stoppage but these were restored in several  minutes and no




    troubles of this nature was experienced recently.







e)  There were 10 cases of stoppage of the rotary valve at the




    bottom of the bag filter (caused by vinyl wrappings etc.)  but




    this type of trobule was overcome by devising a method of




    preventing this type of object from entering the bag filter.






f)  Although there were 11 cases of abnormal operation of the CPU




    where the computer memory was erased due to  a momentary power




    failure, these were overcome by reprogramming.   In addition,




    as a CVCF will be installed during 1978,  reprogramming will no




    longer be necessary.






g)  Although there was a case in August of 1978  in which there was




    a stoppage in the transportation pipeline, the object blocking




    the tube was removed by a vacuum car through one of the inspec-




    tion ports.

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                                                                 59
3.  Design Standards of Pneumatic Conveying Systems of Domestic  Waste





         In order to promote installation of the pneumatic  conveying




    systems of domestic waste in future,  it will be necessary  to




    establish design standards and guide  lines  at the  earliest data.




    For this reason, studies are being conducted on design  standards




    in the survey being carried out this  year.   On one hand, guide




    lines that have already been tested are available  such  as  "Design




    Guidelines for Pneumatic Conveying Systems  (Draft)"  compiled by




    the Japan Association for Environmental Engineering Industry




    (Corporation)  and backed by the Ministry of Health and  Welfare,




    and "Standards for Pneumatic Conveying Systems of  Domestic Wastes




    (Draft)"  as compiled by the Japan  Traffic Planning Association




    (Corporation)  and backed by the Ministry of Construction.




         As design standards may be established taking these guide-




    lines into consideration,  in this  article we shall introduce




    "Design Guidelines for Pneumatic Conveying  Systems"  compiled with




    the support of the Ministry of  Health  and Welfare.
                                - 6 -

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                                                                   60
       DESIGN GUIDELINES FOR PNEUMATIC CONVEYING SYSTEMS (DRAFT)









I.  Basic Plan







1-1  General





          With advancements in urbanization and improvements  in the




     standard of living, the volume of refuse discharged per  unit area




     in the cities is showing an increasing trend.   Although  vehicles




     are generally employed as the system of collection and transporta-




     tion at the current moment,  it cannot be said  that this  is the




     optimum system due to the noise and foul odor  that are generated.




     Moreover, efficiency in transportation has deteriorated  in recent




     years due to increasing traffic congestion.  Also,  as  environmental




     problems are being pointed out around the incinerating plant such




     as traffic congestion and exhausted gas pollution  resulting from




     refuse collection and transportation,  the optimum  means  of access




     to the incinerating plant site has now become  the  subject  for




     acute study.  Also, from the standpoint of city finances,  as the




     costs involved for collection and transportation demands 60  to




     80% of the total budget for  refuse treatment,  and  moreover as the




     cost of labor weighs heavily here,  the pressure of increasing




     costs for collection and transportation on the total refuse  dis-




     posal budget can be said to  be extremely high  when we  consider




     future increases in labor costs.




          This pneumatic conveying systems  of refuse (hereafter referred




     to as "pneumatic conveying systems")  is one  form of improvement




     measure that was considered  to resolve the problem points  of the
                                 -  7  -

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                                                                  61
     current system just explained and it is anticipated that this will




     result in improvements in standards of comfort and sanitation




     during collection and also in economizing in labor costs.   As




     there are cases of practical usage of this system in foreign




     countries, it is believed that this will become popularized in




     our country as a practical means of improving our urban environ-




     ment and our refuse disposal process.




          Although future efforts are anticipated from various  sectors




     for healthy growth of garbage control facilities,  it will  give




     us great pleasure if these design guidelines will  serve as an




     aid in any way.









1-2  Basic Policy





          It will be desirable that detailed studies be conducted in




     relation to the following items in designing this  facility.






     (1)   Sorting and Selecting





               Intoduction of a sorting device and a selecting  device




          in this system should be considered from the  viewpoint  of




          processing,  final disposal and reclamation.






     (2)   Overall Disposal Plan





               Suitable measures must be considered for refuse  not




          collected by this facility.







     (3)   Operation and Administration System





               An operation and administration system should be
                                - 8 -

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                                                                62
          considered for this facility including a  rate  system.









1-3  Basic Plan





     (1)   Target year of the plan





               As a basic rule the  target year of the plan shall be




          15 years.






     (2)   Area covered





               The following items  shall be considered in determining




          the area to cover.






          (a)   As a basic rule,  the planned area shall be the area




               forecasted to be  urbanized by the target  year of the




               plan.






          (b)   The planned area  shall  be determined comprehensively




               irrespective of administrative boundaries.






          (c)   Facility  planning for newly developed urban areas must




               be implemented as a  part of the overall domestic waste




               treatment plan for the  existing urban areas.






     (3)   Planned population





               The planned population  must be determined based on the




          following items predicting the development conditions within




          the planned area at the target year of the plan.
                                -  9 -

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                                                               63
     (a)   Estimation of the total planned population





               The total planned population is determined by




          estimating the population for the target year  of the




          plan based on past population growths and,  moreover,




          taking into consideration population growth in areas




          where sharp growth is predicted.







     (b)   Estimation of population distribution





               Population distribution  within the  planned area




          shall be determined by using  population  density by




          planned land usage as reference and distributing the




          total planned population.







(4)   Planned volume of refuse





          The planned volume of refuse  shall  be determined based




     on the  following items.







     (a)   Planned daily discharge  volume





               The planned daily discharge volume  shall be  fore-




          casted by using refuse discharge per  unit source by




          usage of the  structures  as reference.






     (b)   Planned maximum daily  discharge volume





               1.2  to 1.3 times  the planned daily discharge




          volume  shall be considered the criterion.







     (c)   Planned maximum daily collection volume




              The planned maximum daily collection volume shall










                           - 10 -

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                                                                    64
               be the total amount of maximum planned daily discharge

               volume within the collection area.   However, where

               daily collections are not made, the amount will be

               increased based on the number of planned collection

               days.
II.  Design
II-l  Guidelines in relation to the environment and safety factor of
      the system
      (1)   Water drainage countermeasures


                Water discharge must be in compliance with the water

           pollution prevention law (Law No.  138,  1970).


      (2)   Noise countermeasures


                Noise must be in compliance with  the noise control

           law (Law No.  98, 1968).


      (3)   Foul odor countermeasures


                Foul odor must comply with regulations under the foul

           odor prevention law (Law No. 91, 1971) .


      (4)   Dust countermeasures


                Dust must be in compliance with  the basic  pollution

           control law (Law No. 132, 1967).


      (5)   Vibration countermeasures


                Significant vibrations shall  not  be applied to other

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                                                                   65
           facilities.







      (6)  Disaster countermeasures





                Proper measures must be taken against disasters such




           as fires, wind and water, earthquake and ground subsidence.







      (7)  Safety and security countermeasures





                Safety measures must be taken into consideration when




           determining the position, shape and dimensions of the




           refuse post and other portions and security measures must




           also be taken such as using manual or automatic locks.









II-2  Guidelines in relation to the basic design







      (1)  Air transportation





                This is a suction or pressure system in which refuse




           and air are mixed in the tube and refuse is transported




           with the air flow in the tube.






           (a)   Air volocity (m/sec)





                     Shall be designed for air velocity of 20 to 30 m/sec




                as the standard so air transportation functions can be




                fully displayed.






           (b)   Mixture ratio





                     A mixture ratio under 3 is desirable from the




                standpoint of preventing stoppage of the transportation




                tubing with refuse.
                                 -  12  -

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                                                             66
           .  .       ..     Amount of refuse to be transported (kg/sec)
          Mixture Ratio =	—	:	%~.	-r.—,   .	
                            Amount of air for transporting (kg/sec)
     (c)   Tube diameter (mm szf)




               As a basic rule,  the transportation tubes shall



          be designed with a diameter of 400 to 600 mmjzi.



          However, this may be increased or decreased in relation



          to the quality and volume transported.





     (d)   Motive power for the system (Blower)




               The motive power  for the system must be designed



          with a reserve shaft output of approximately 20%.





(2)   Capsule transportation





     (a)   Transporting speed




               To enable this'system to display its functions to



          the fullest, it is designed for a transporting speed of



          5  to 15 m/sec.





     (b)   Tube diameter




               The transporting  tubes shall be designed with a



          diameter,of from 600 to  1,600 mmjzi.  Depending on the



          quality and volume of  the refuse, however,  this will



          not apply.





     (c)   Required power




               The percentage of reserve power shall  be 20%  of



          the calculated necessary power.







                           - 13  -

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                                                                 67
II-3  Guidelines in relation to constructional design


      (1)   Air transportation


           (a)   General items


                     The general structure of the pneumatic  conveying

                system must conform with the following requirements.


                1)   Must safely withstand its own weight,  snow load,

                    ground pressure,  wind pressure,  earthquakes,

                    vibrations, and climatic changes such  as heat and

                    cold.
                2)   The components in this system must  possess
                    sufficient durability.
           (b)   Inlet Portion (Disposal port,  dust chute)


                     As the diameter of the connecting  pipe between

                the inlet portion and the transporting  tube is  less

                than that of the transporting  tube,  it  must be  con-

                structed in such a manner as to  prevent stoppage  from

                occurring.  Further, the inlet portion  must have

                airtight characteristics for safety,  anticorrosion  and

                prevention of odor and thorough  consideration should

                be  given to disaster prevention  and  security devices.


           (c)   Discharge valve


                     The discharge valve possesses airtight character-

                istics to maintain pressure within the  tube and must
                                - 14 -

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                                                      68
     be high performance types  to  enable  smooth suction of




     the refuse in the  dust chute  into  the  transporting




     tube when this valve is opened.  Further, it must be




     of rugged construction to  withstand  the  shock of any




     form of refuse dropped through the disposal port.







(d)   Bends and inclination angle of joints





          The standard  radius of curvature  of bends shall




     be more than 4 times the diameter  of the transporting




     tube.  However,  this shall not apply in  special cases.




     Branch tubing and  collective  tubing  shall be designed




     in accordance with the foregoing.  20% should be used




     as the criterion for the inclination angle of elevation




     when designing.






(e)   Types of transportation tubes





          As a basic  rule,  steel pipes  shall  be used as the




     transportation tubing and  the straight portions that




     are not subjected  to ground pressure shall be designed




     with a thickness of over 6 mm.






(f)   Inspection port





          The system shall be designed  to provide inspection




     ports when necessary at places where blockage of the




     tubing or accumulation of  garbage  can  be anticipated.
                      -is-

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                                                          69
 (g)  Method of laying





          When burying the tubing, 1 meter shall be considered




     the standard depth.  Special protective measures must be




     taken for any depth less than this.  However,  this is




     not applicable where surface loads need not be considered.




     Further, electrolytic corrosion prevention designing




     must be carried out on places prone to corrosion




     (asphalt_corrosion prevention etc.) or any other places




     felt necessary.




     Noise prevention should be taken into consideration




     when designing exposed portions of the piping.




     Where public roads are involved, designing must be




     carried out after consulting with the road supervisor.







 (h)  Blower





          Thorough noise prevention measures must be taken




     When designing the blower.  When using a turbo  system,




     it will be necessary to incorporate an airflow  adjusting




     device in the design to maintain a constant air speed




     in the tube.




          Where necessary,  a spare blower should also be




     incorporated in the design.






(i)   Separator





          The construction  of the  separator  should be




     designed for superior  separating performance.
                     -16-

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                                                       70
(j)   Dust collector





          As the air will contain mist and dust after the




     waste is separated in the separator,  a dust collector




     must be incorporated in the design to discharge clean




     air into the atmosphere in accordance with the basic




     pollution control law.   It should also be designed for




     long years operation and constructed  for ease in




     maintenance and control.







(k)   The device to discharge refuse





          The device to discharge refuse from the separator




     should be designed for high reliability to prevent




     trobule and stoppage due to adherence of refuse.







(1)   Muffler





          A muffler should be incorporated in the design to




     hold noise level down to the value prescribed in the




     pollution control law when discharging air into the




     atmosphere.






(m)   Deodorizing Device





          As foul odors in the air used for transporting




     refuse must be held down to the  value prescribed  in




     the foul odor prevention law before releasing the air




     into the atmosphere,  it will be  necessary to incorpo-




     rate deodorizing devices in the  design.
                      -  17  -

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                                                                     71
     Current  State  of Pneumatic  Conveying Systems  of Domestic  Waste
                   Discussion Leader:  Mr. Akio Namiki
 Question:   You stated that  in  July,  1978,  a survey was  conducted  of  the
            user by means of a  questionnaire,  and  that 1C% of  the  users
            commented  that it was  inconvenient and bothersome  as the refuse
            post must  be  locked, the  distance  of the  post  is too far,  and
            there is a limit to the size  of the material the system will
            handle.  What is the average  distance  to  a refuse  post?
 Answer:     Our highrise  apartments have  generally six or  seven stories,
            and each story has  a refuse post;  so the  distance  is 20 meters
            at  most.
 Question:   How does the  locking system operate?
 Answer:     Each story has 9 or 10 family units and each family has its
            own key.
 Question:   What is  the maximum size  of the material  that  can  be put into
            the system?
 Answer:     The size of the  material  should be less than 50 centimeters in
            diameter because the pipe is  50 centimeters  in diameter.
 Question:   What do  the residents  do  with larger materials?
 Answer:     The bulky  items  are treated differently.
 Question:   What about the weight  e.g., glass  jars... Can  you  put  anything
            into it  that  will fit?
 Answer:     Yes,  they  can take  almost anything provided  it  is  the  riaht size,
            including  glass  jars.
Question:   What is capsule transportation?

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                                                                    72
Answer:    Capsule transportation is still in the experimental  stage;  it




           has not yet been put into practice.   Put we are thinking of




           using  capsule transportation for secondary transportation e.g.,




           from collection sites to final disposal treatment facilities.




           At this point in time we are using tracks to transport collected




           waste to final disposal facilities but we would like to replace




           it with a conveying system with capsules.




Question:  What size capsule?




Answer:    6 centimeters in diameter  and   I centimeter in length.




Question:  Is that the size for the experiment or it that the size in




           the final installation?




Answer:    We have not come up with the final figure yet.




Question:  Why is volume of waste used as a design factor not density?





Answer:    Simply because we are dealing with domestic waste which contains




           glass jars and cans and not heavy metals.




Question:  In the Port Town experiment, were there any problems with odor




           or noise?



Answer:    At this point I can say that there have been no problems what-




           soever with odor or noises.




Question:  How does the discharge drum operate?




Answer:    When the discharge drum accumulates after a certain point




           then there is a sensor attached to it—it is all computerised—




           so that when it is filled  it is  automatically pushed into




           conveying pipes.

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                                                            73
1.    Status  Report
    1-3    Location Problems of Refuse Treatment Facilities
                           by



              Shiro   Kawaguchi



              Professor  of  Sanitary  Engineering



              School  of  Civil Engineering



              Faculty of Engineering



              Tokyo Metropolitan University

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                      Contents
     Synopsis
1.   Introduction
2.   The calculating procedure
3.   Solution of a sample problem
4.    Summary                                                 10
     Appendix;  The linearity of the transportation cost      12
                              -1-

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                                                                         75
                            Synopsis
    In this paper, a solution method of location prv.,_ouis is discussed. The
object to solve location problems lies in finding the economically optimal
locations of refuse treatment facilities.
    Several solution methods which appeared in literatures are reviewed.
Those methods which were described by Cooper, Hakimi, Maranzana and Teitz et
al. are necessary to explain the heuristic method presented here. In this
method,the actual service area is transformed into a graph.
    It is the essence of this method that fixed charges are introduced into
the object function to represent non-linear costs for the construction of
facilities.
    After solution procedures have been explained, a sample problem which
is constructed on the map of a city is solved demonstratively,  to find the
optimal number of facilities and their locations.
                                     -2-

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                                                                        76
 1.   Introduction




     Location problems are constructed to locate many kinds of central facilities




 which have service points dispersed on the object area. Examples are warehouses,




 distributing centers, communication centers, factories, refuse incinerators




 and so on.




     In the most general location problems, if the locations of target points,




 the demand of each target point,the transportation costs and the facility costs




 are given, the number, the location and the capacity of the supplying facilities




 must be answered. In case of transportation costs not having directions, target




 points and supplying sources ean be exchanged mutually; in other words, the




 case in -which goods are distributed from warehouses to stores is similar to




 the case in which refuse is hauled from homesteads to incinerators.




     It is important to know the economically optimal locations of the central




 facilities, not only in cases in which the facilities have not been established




 yet and must be installed hereafter", but also in cases in which the facilities




 have been established and are operated, because we can compare the present




 locations to the optimal and evaluate the merit of the present locations.




     Following to the comments by Leon Cooper  , "in the purely mathematical




 literature this location problem is a very old one. Cavalieri in 1647 considered




 the problem of finding the point the sum of whose distances from three given




 points is a: minimum. Heinen in 1834 noted that in a triangle, which has an angle




 of 120 degree, that the vertex of this angle is itself the minimum point.




 Fagnano in 1775 showed that the point for which the sura of the distances from




 the vertices of a quadrilateral is a minimum is given by the intersection of




 the diagonals. Tedenat in 1810 found for thecase of n points the following




necessary condition: The sum of the cosines of the angles between any arbitrary




 line in the plane and the set of lines connecting the given points with the




minimum point must equal zero. Finally, Steiner proved in 1837 that the necessary




and sufficient conditions are that the sum of the cosines and sines of the above




mentioned angles be zero."



                                      —3—

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                                                                      77
                           2)
      According to a review  ,  location analysis began with Weber who considered


 the location of a factory between two resources and a single market. Beginning

                                1)                     3)
 with the formulations of Cooper  ,  and Kuhn and Kuenne  ,  interest in location


 analysis quickened.  Their works described an iterative process  for solving the


 generalized Weber problem and  their Solution method is classified as the locational

                                    4)
 equilibrium model in another review


      To handle this  kind of problem,  an algorithm is needed which can solve the


 group of problems characterized as  the plant location problem.  Other several


 suggested approaches,  different from the locational equilibrium model, might


 be classified as  linear  prog-ramming with or without fixed  charge and heuristic


 methods.  Linear programming which assumes both  a linear objective function


 and linear constraints may be  solved  using a well established and tedious  com-


 puting procedure  which may become very big for  actually meaningful problems.


      Cooper also  pointed out the importance of  heuristic methods  and presented


 a  computing procedure  which stimulated other researchers and became a base of


 recent distinguished heuristic  methods.  Kuehn and Hamburger   devised a heuristic


 method by  which they solved a so-called warehouse problem whose  object is  to


 find  the optimal  locations  of warehouses.  Feldman,  Lehrer and Ray   rearranged


 the method of Kuehn  et al.  In the method of  Kuehn et al., a warehouse is located


 as  the initial  condition on the designated  plane  and another warehouse is  added


 one by one, until the  optimal number  of warehouses  is  found. In the method of


 Feldman et  al., contrary  to  the former method, all  possible warehouses are


 located initially on the  plane,  and one  of  them is  dropped from the  set of


warehouses by one at a time, until the optimal locations are found.

            J\   Q\
     Hakimi      introduced  the  graph in  location problems, not using the plane


on which facilities should be located. It is called Hakimi's theorem  that


there must be the optimal locations to which the  total distance of transportation


become minimum on the graph and  each location must be on one of the nodes of the
                                    -4-

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                                                                          78






 graph.  In  case  of  p  facilities  to be located, the set of the p optimal  locations




 is  called  p-node-median by Hakimi who did not present any elegant algorithms




 to  find it, but calculated the  total distance of all combinations taking the




 set of  p nodes  out of nodes of  the given graph, and compared each total distance




 to  other to find the shortest.  This simple method of finding p-node-median  is


                                                    9)
 refined in the  substitution method by Teitz and Bart  , who initially pick  up




 from the nodes  of  the given graph p arbitrary nodes one of which is then replaced




 to  find the optimal set of p nodes by a node which has not been contained in




 the initially taken set of p nodes and so on.




     Maranzana    solved a sample problem by a similar method to Cooper's




 iteratively calculating procedure, using a graph whose nodes are forty Italian




 cities  and should be divided into three blocks.  Quoting the excellently brief


                           2)
 words on Maranzana's method  ,  " The algorithm begins with the arbitrary selection




 of  p of  the n nodes to serve as sources. The remaining n - p nodes are partitioned



 into p  subsets  such that each nodecis assigned to its closest source. For each




 subset,  a single node is isolated Which minimizes the sum of the transport costs




 to  all nodes of  the subset.  Maranzana refers to this node as a local center




 of  gravity. The  centers of gravity are chosen as the new sources.  The nodes



 are repartitioned,  the centers of gravity located and compared to  the previous



 designation and so on.  If all the centers of gravity coincide with the previous



designation of sources,  the algorithm terminates." Maranzana's method looks




more charming than that of Teitz et al., but from the view point of computer



programming the latter method is thought to be simpler.




     Other authors  except Kuehn et al.  and Feldman et al.  did not  introduce




 the  costs of facilities but only considered transport costs.  To find the optimal




number of facilities, it is  necessary to introduce the costs of establishing



 facilities which are conveniently formulated as  fixed chrges in linear programm-




 ing. Also in heuristic methods using graphs, the costs of  establishing facilities
                                    -5-

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                                                                    79





 could be incorporated conveniently by considering weights which are designated



 to describe the costs and are burdened to each of nodes on which a source should



 be assigned.  We refer to these weights hereafter as  center-node-weights ( C.N.W.),



 In this case, the criterion is to minimize the sum of transport costs and the



 C.N.W.   In this paper,  the solution of a sample problem is described, connecting



 to location problems of refuse treatment facilities,  by a heuristic procedure



 accompanying C.N.W.



 2.    The calculating procedure



      On which specified nodes of  the graph,  the treatment facilities should



 be located, minimizing  the costs  of transportation,  construction and running



 of the  facilities, will be considered henceforth.



      It is assumed that in the first the refuse quantity generated  from each



 portion of the object area has an area stability;  in  other words,  the ratio of



 the refuse quantity  generated from a portion of the object area  to  the  one from



 another portion does  not change.  In the second, we assume  that  the  cost of



 transporting  refuse  from each of  portiers  of the object  area to  one of  the



 facilities is  described by a  linear  equation wJiose variable is  the  mean hauling



 time  and whose coefficients are constant over  th-i  whole  object am. (  See the



Appendix in the  end of  this paper.)  In this case,  the problem is  the single



source  problem,  because the refuse  from one of  the portions of the  object area



is hauled  to only one facility. Thus,  to locate multiple,  say, m facilities



in the  object  area means  to partition  the area  into m  blocks.



     We initially divide  the object  area into n portions; P , P  ,...,P  . Each



portion generates refuse of wn, w_,...,w  in weight respectively. The m blocks
                             l   /      n


are Q,, Q0,...,0 . Then we consider  the object area to be a graph whose nodes
     Li      m


are equal  to the n portions.



     The formulation of the problem  is



         Minimize      cDX'  +  FK
                                    -6-

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                                                                     80
          Subject to:
                      x..  = w.  or  0




                      3-1 xij  = ^ Q.xij


                      k. = 1  if P. is the center, otherwise 0.


 in which X'  is  the  transposed  matrix of X whose element x.. denotes refuse


 weight hauled from  a  node P. to a node P. ; F  is a row vector whose element  f.


 is the C.N.W. set on  the  node  P ; K is a column vector whose element k.  is 1


 or 0;  D is  the  distance matrix whose element d.. denotes  the distance  of the


 shortest path from  a  node P. to a node P.; and c is a conversion factor.


     A node. P.  is called  a center, if a facility is set on it. In usual  cases,


 d..  =  d..,  that means that the distance from P. to P. equals the one from P.


 to P±.


     If w..  = w« =,..= w , that is, in the partitioning of the object area, each


 refuse quantity generated from all the portion equals other, the formulation


 should be changed slightly:


                             Vn        ••
                             LA-I x-• = 1



                             x.. = 1  or  0.


 In this case, the conversion factor c must have a different value from the


 former.


     The successive parts of the calculating procedure are the following:


        Step  a.  Partitioning  of the object area and constituting all the  portion



                as nodes into a graph;


        Step  b.  Making up  the distance matrix;


        Step  c.  Finding the optimal nodes.


 In the following sample problem, Step a has been done manually; Step b and c


by computerized  calculation.
                                    -7-

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                                                                      81
 3.   Solution of a sample problem




      A sample problem is constructed on the map of Kawasaki city which has




 population of about one million persons and three operating incinerators  and




 one incinerator under construction.




      To make up a graph, the city area has  been partitioned into seventy  eight




 portions,  each of which generates refuse quantity of  twelve ton  daily  on  the




 basis of mean daily discharge.  The distance between two  adjacent portions




 means the  one between the two central points each of  which  is  looked to be  in




 the central part of each portion and is measured along main roads on the  map.




 Hauling routes are constructed  to be the shortest path between one portion  and




 another. Hauling vehicles go along these routes to one of the  center nodes




 after collecting the refuse deposited on each of portions.  In  shorter words;




 Nodes mean central points of portions;  Links mean paths  between  adjacent  nodes;




 Routes mean the shortest sequential  combinations  of links between two nodes.




      If there is not  scale economy in costs  of  establishing  an incinerator




 and  the direct costs  of  constructing  and "operating the incinerator are  in pro-




 portion to  refuse quantity treated at  that site,  it is appropriate to assume




 the  sum of  costs of buying land  of the  site  and  costs for special construction




 works  necessary to  the site  to be  a  fixed charge  assigned to the  construction




 site.  In this  paper,  thus  assumed  fixed  charge  is  called C.N.W. which is  assigned




 to each of  nodes  of the  graph. It  is a very  difficult matter to decide exactly




 the  absolute value of each of the  C.N.W.s in conformity with the absolute values




 of linear costs,  such as hauling,  constructing and operating costs which are




 thought to be  in  proportion  to refuse quantity handled.  But in this situation,




 fortunately, there is a  suitable method of assigning C.N.W.  to each of  nodes.




 In this method,  the value  of the assigned C.N.W. to P. is assumed to be near




 the value of the  sum of weighted transportation distances over Q. which includes




P..
 i

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                                                                         82







      By  the results of several calculations on the sample problem, the effect




 of  the value of C.N.W. to the deviation of the center nodes is not so large




 that  exact determination of the values of C.N.W.s is not necessary, especially




 for the  purpose of estimating the optimal number of facilities. In this case,




 the value of C.N.W. assigned to each of nodes is determined nearly in proportion




 to  the population density in that portion, considering that the population




 density  may govern the value of C.N.W., that is, a measure of the difficulty




 of establishing a facility on that site. Also, to fifty percent of thus decided




 values of C.N.W.s, the problem is solved.




      Figure 1 is a sketch of one of calculation results done on the seventy




 eight nodes graph. In this case, the designated C.N.W. is weighed on each of




 nodes. The numbers of the optimal center nodes are 14, 29 and 60 as a result




 of partitioning into three blocks, whereas without C.N.W. 6, 38 and 60. The




 actually operating incinerators are on nodes 3,  18 and 77.  When fifty percent




 of the prescribed C.N.W.  is weighed on each node,  the center nodes are 12, 38




and 60.  It is expected without any calculations, because of moderate values




of C.N.W., that the center nodes deviate slightly in this manner in accordance




with the changes of the values of C.N.W.




     In Figure 2,  it is seen quickly that the total distance which means the




sum of the total weighted hauling distance and the total value of C.N.W.  de-




creases generally in accordance with the growth  of blocks,  that in case without




C.N.W. the total distance decreases monotonously and that with C.N.W. it de-




creases slowly,  but especially in case of the prescribed C.N.W. the decrease




stops when blocks grow to four.  The above observation seems to justify the




idea which  the optimal number of blocks can be  found by adding C.N.W.  of some




values to each of nodes and we can say that in this sample problem the optimal




number of blocks is four.
                                    -9-

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                                                                     83
  4.    Summary

       This  paper briefs  the heuristic method  utilizing a  graphical notion of

  finding  the optimal number of  facilities which must be established  for  the

  purpose  of the public cleasing service  of  that city. This method mainly consists

  of  two parts: in  the first,  the  optimal locations are found  to the  fixed

  number of  facilities and  the total distance  necessary to hauling and  settle-

  ment  of  facilities are  accumulated; in  the second, the first solution proce-

  dure  is  once more executed to  another fixed  number of facilities and  so on.

  When  a set of the total distances is attained, the final work is to select the

  number of  facilities to which  the total distance must be near the miniaum.



       References

  1)  Cooper, L. (1963). " Location - Allocation Problem", Operations Research,
     Vol.11, pp. 331 - 343.
  2)  Marks,  D.H., C.S. ReVelle and J.C. Liebman (1970). "Mathematical Models of
     Location:  A Review", Journal of the Urban Planning and Development Division,
     Proceedings of A.S.C.E., Mar., pp. 81 - 93.
  3)  Kuhn,H.W.  and R.E. Kuenne (1962).  "An Efficient Algorithm for the Numerical
     Solution of the Generalized Weber Problem in spatial Economics", Journal of
     Regional Science, Vol.4, No.2, pp.21 -33.
  4)  Helms,B.P. and R.M.Clark  (1971).  "Locational Models for Solid Waste Manage-
    ment",  Journal of the Urban Planning and Development Division, Proceedings
     of A.S.C.E.,April, pp.1 -13.
  5)  Kuehn,A.A. and M.J.  Hamburger (1963). "A Heuristic Program for Locating
    Warehouses", Management Science,  Vol.10, pp.643 -668.
  6)  Feldman.E., F.A.Lehrer and T.I.Ray (1966). "Warehouse Location under Con-
     tinuous Economies of Scale", Management Science,  Vol.12, No.9, May, pp.670-
     684.
  7) Hakimi,S.L. (1964).  "Optimum Locations of Switching Centers and the Absolute
    Centers and Medians  of a Graph",  Operations Research,  Vol.12,pp.450-459.
 8) Hakimi,S.L. (1965).  "Optimum Distribution of  Switching Centers in a Commu-
    nication Network and Some Related  Graph Theoretic Problems",  Operations
    Research,Vol.13,  pp.462-475.
 9) Teitz,M.B.  and P.Bart (1968).  "Heuristic Methods  for Estimating the Generali-
    zed Vertex Median of a Weighted Graph",  Operations Research,  Vol.16,  pp.
    955-961.
10) Maranzana,F.E.  (1964).  " On the Location of Supply Points to  Mininize Trans-
    port  Costs",  Operational Research  Quarterly,  Vol.15,  No.3, pp.  261-270.
                                    -10-

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                                                                     84
Fig.  1   A Graph of Seventy Eight Xodes
800
E
1 40°
0



r—

t
\
\






\



—

x


I 2 3
Num
•
- U nhoui C N
- V, uh C N V.
-\\ ilh CN'.W.

KT






•~~
. •

— —


-.
• —


-
^

vV.
of 50%


5 6 7 8 9 10
>er of Blocks
 I7ii». 2  Total Distance vs. Numbers of
        Block,
                     -11-

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                                                                     85
 Appendix
 The linearity of the transportation cost


     The transportation cost including refuse collection cost  has  many  kinds
 of components.  But its main components are man-power,  vehicle costs  (  fuel,
 repairment,  insurance and  miscellaneous material  )  and amortized  cost.  For
 example,  in  Kawasaki city  public  cleansing service,  the sum of these constituting
 costs  was 94.4  % of the total cost  of the refuse  transportation in 1973. Wu
 can assume that the transportation  cost is proportional to the number  of the
 vehicles, because the main part of  the cost is  thought to be  proportional to
 the number of the vehicles.
     We consider the number of necessary vehicles  to  collect and transport the
 refuse from  a service area where  there are F homesteads. We divide the  area
 into m portions.  Each portion is  denoted by D.  where there are F. homesteads,
 (  i -  1,  2,  I..,  m ).
     It is assumed that the refuse collection work for  the portion D. can be
 described by the  following simple equation,
     Q  = C[ T -  (  t2  + t3 + t4 + t5  )]  /  [  C p + ( C  /  q - 1 )  tj + t& + t1 ]
 in which  Q is the refuse quantity collected and transported in a day by a
 vehicle,  kg;  C, allowable  load to a vehicle,  kg; T,  working time in a day, sec;
 t_  , time from  the garage  to  the  first  picking-up point, sec  ;  t~, time for
 lunch,  sec;  t,  ,  rest  time, sec;  t_,  time  for vehicle washing,  taking bath,
 reporting and other  off-route time, sec; p,  time for picking up 1 kg refuse
 at  the  picking-up  point, sec/  kg; q,  refuse  quantity deposited  at each  picking-
 up  point,  kg; t1,  time  from a picking-up point  to the next, sec; t,, time for
                                                          i
 measuring and dumping  refuse  at the treatment site,  sec; t ,  return transporta-
 tion time from D.  to  the treatment site, sec.
     In  the first,  we get the  following relation,
            Hi fl  «1 = «l.
 Here, H.  is the hauling times  necessary  to collect refuse from  the D. ; f ,  the
 number  of homesteads equivalent to the allowable load of a vehicle considering
 the refuse discharge from  the  homesteads which  is assumed to  be q. kg per
 homestead daily; Q., the refuse quantity collected from the D. by a vehicle
 daily.
    Next,  we get the following relation,
            f - q, = Q..
             vi  u   xi
Here, f .  is  the number of homesteads in D. served by a vehicle.

                                       -12-

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                                                                      86
    Moreover, we see that f.. q1 = C. Hence, we get  the  following  equation,
 fvi=  [T -(t2+ t3+t4+ t5)] f1 / [ (qlP -f fl) fx+ tg+ t1 ]
in which n is the number of homesteads belonging to a picking-up  point.
    If we write that [T - (t2+ t + t,+ t )] f^ = a  and  (q p + _^1)  f  + t  =
b, the above equation becomes
             fv± - a / ( b + t1).
    We assume that the a and b are independent on i. The number of vehicles
necessary to a homestead, v,., is
             vfi = 1 / fv± = ( b + t1 ) / a.
    Hence, the number of vehicles necessary to the whole area, N,  is
      N ' lll Vfi Fi - I { b F + SI=lFi tl}-
The number of vehicles necessary to each homestead,vf,  is represented  by  the
following equation,
             vf - N / F - i { b + Zj^ t1/ F } .
in which  Z F. t  is the mean return transportation time. Hence, we can say
that the number of vehicles necessary to a homestead in some area  is given
by a linear equation whose variable is the mean return  transportation  time.
                                      -13-

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                                                              87
             Location Problems of Refuse Treatment Facilities
               Discussion Leader:  Dr. Shiro Kawaguchi
Question:  In our discussion of the sample problem, each node was chosen
           to represent 12 tons per day.  Does this represent the daily
           capacity of one collection vehicle?  If so, are these actual
           routes or hypothetical?
Answer:    No, this figure comes from the fact that we divided the city
           into 78 nodes; that is why we came up with this figure of 12
           tons per day.  These are hypothetical routes.
Question:  The sample problem was concerned with locating incinerators.
           Is it also possible to use this procedure to locate a mixture
           of facility types?   For example, incinerators and pyrolysis
           plants?  Can this procedure be used in an iterative fashion to
           locate various types of processing?  For example, transfer
           stations which haul to incinerators which then haul residue
           to landfills?
Answer:    Yes,  it is possible to use this procedure to locate a mixture
           of facility types.  However,  based on our experience,  it is much
           more difficult to use this procedure to differentiate between
           facilities of the same type.
Question:  Your graph in Figure #2 illustrates how the total transport
           distance decreases to a point and then levels off.  It appears
           that there are numerous arrangements which are close to the
           minimal distance.   In this case,  it appears that the economics
           of scale associated with a particular facility would be a

-------
                                                                         38
           major determining factor in finding the optimum number and loca-




           tions of such facilities.   Do you agree?




Answer:    Yes, I  agree.   My research to date indicates that the economics




           of scale do not exist.   In reality, I think our general  im-




           pression is that economics of scale does not exist in the




           field of incinerators and  waste treatment facilities.   It




           appears that economics of scale is that amount of waste




           covered by the facility  proportional to the size of the




           facility.   In other words, what we are saying is that there




           appears to be no economics  of scale in existence. That




           means it does not matter what the size of the facility is.




           The reason why there is no economics of scale in existence




           in Japan is that those big facilities tend to be located in




           major cities where the administration costs are very high.




Question:  Has this method of locating facilities been used in Kawasaki




           City or any other city in  Japan?




Answer:    We just used this method in Sapporo.  However, we have not used




           it anywhere else.




Question:  In the United States there have been many attempts to logically




           locate refuse facilities in a manner that is economically viable




           and environmentally sound.  However, most often the final decisions




           are made under intense social and political pressure because




           citizens do not want a facility located near their homes. Dt> you




           encounter  similar problems  in  Japan?  If  so,have you  found  any solutions?




Answer:    Personally I do not encounter these problems, because I am a

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                                                              89
           professor at a university.  But I understand that we have the same




           problems in Japan.  I would be very happy if I could say that we




           have found some solutions.




Question:  Do you feel that an economic approach like this might enhance




           public acceptability of such a facility?




Answer:    I don't think that this economic approach will have much of an




           impact on what basically is a political decision.

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                                                     90
1.  Status Report
     1-4.   Removing HC1  gas  in the exhaust from



           a refuse incineration plant






             -  A case  of Yokohama City -
                  Takashi  Miyanohara






     Research Institute  of Solid  Waste  Management,





            Environmental  Cleaning  Bureau,





                     Yokohama  City

-------
                                                                 91
                         CONTENTS

                                                            Page
1.  Present status and future trend of waste
    treatment work in Yokohama City	     1

2.  Regulation of exhaust gas from
    refuse incineration plant	     3

3.  Present status of HC1 from refuse  incinerator   ....     6

    3-1.  Present status of HC1 discharge  according
          to  the  qualities  of refuse  	     6
    3-2.  Pres.ent status of HC1 discharge according
          to the types of refuse incinerators  	     9

4.  General description of the technology for
    removing HC1 from refuse incineration plant  	   10

5.  Measures for removing HC1 and their efficiencies 	   13

    5-1.  HC1 removing efficiency in  the wet type
          simplified scrubbing method  	   13
    5-2.  HC1 removal efficiency of the method of
          atomizing alkaline into the  incineration
          furnace 	•.	   17
    5-3.  HC1 removing efficiency of  the dry type
          alkaline solution atomizing  system 	   21

6.  Evaluation and conclusion 	   23

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                                                                   92
Removing HC1 gas in the exhaust from a refuse incineration plant

                    - A case of Yokohama City -

1.   Present status and future trend of waste treatment work in
    Yokohama City.

         Yokohama City has about 2.7 million population,  and the
    number of households is 810 506.  672 881 tons of household refuse
    and 23 344 .tons of bulk waste were discharged in 1977 from all
    these households,  the total volume of which was collected by
    the city administration.
         As-to the frequency of collection,  54.8% and 45.0% of the
    household refuse are collected twice and three time a week re-
    spectively,  while  0.2% is collected every day.   The bulk wastes
    are collected once every 1.5 months.   There are also  the wastes
    collected from the roads,  rivers,  parks  and factories of medium
    and small sizes.   The city has treated total 918 104  tons of
    wastes including all of the above  in the year.
         The 74% of these wastes was burnt by the continuous type
    incineration plants  at five locations, while the remaining 26%
    was disposed of by the land reclamation  at three places together
    with the burnt residue.   The amount of the burnt residue is about
    20% weight of the  wastes  to be treated since glass bottles,  cans
    and other incombustibles  are included in the household refuse.
         As you  see in Figure 1,  the population and the amount of
    wastes are showing the increasing  tendencies,  however,  there is
    only a limited area  of ground to be used for land  relamation in
    the city.  Therefore,  it  is decided to construct additional in-
    cineration plants  to promote the disposal of wastes by inciner-
    ation.
         On the  other  hand,  the legal  control is being enforced a-
    gainst the disposal  by incineration on the viewpoint  of the en-
    vironmental  protection,  accompanying  the increased cost for waste
                            - 1 -

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                                                              93
disposal.  We are making efforts for the promotion of utili-
zation of the wastes with the reduction of waste amount and
the application of the waste heat utilization (electricity
generation, steam supply to the regional community) as well
as the research and development of the waste utilization.
     Such consideration is a common concept among a large num-
ber of cities in Japan.
100 -
(xlO"t
Waste)
(xlO"
House-
holds)
50 -








-

7
/;
''




-

;-
^

'-




*

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/

-* *



'*?

7
/




i — |
^*-

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/





—

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'/
/





::^.

^
/
;/






i
i"' •
^
/
/







,
s_
7
^
^
/
,_ I
E

	 N

•*— I

                                                Incineration
                                                Residue •* Land
                                                 reclamation
                                                Land reclamation

                                                No. of households
                                                Incineration
       1969 '70 '71 '72 '73 '74 '75 '76 '77 '78
     Fig. 1  Trend of numbers of households for waste
             collecting and waste amount (Yokohama)
                         -  2  -

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                                                                94
2.  Regulation of exhaust gas from refuse incineration plant
         As to the exhaust gas from a waste incineration plant,
    the kinds and the standard levels are provided in the provi-
    sions of the Air Pollution Control law.  A waste incineration
    plant should be operated by controlling the exhaust gas under
    the levels provided in the law.  At present, the controlled
    items and their standard levels are shown in Table 1.
             Table 1.   Regulation.standards for exhaust gas
                       discharged from a waste incineration
                       plant
Items
Control
level










Remarks









Dust
Continuous fur-
nace
0.2g/Nm3
or low-
er

Special
standard
O.lg/Nm3
or
lower,

When
the
exhaust
gas is
larger
than
40 000
Nm3/h.


0.7g/Nm3
or low-
er

Special
standard
0.2g/Nm3
or
lower,

When
the
exhaus t
gas is
smaller
than
ko ooo
Nm3/h.


Others
0.7g/Nm3
or low-
er

Special
standard;
0.4g/Nm3
or low-
er











sox
q(Nm3/h)
or low-
er by
the ecu—
ation
q=KxlO~3x
He*
He: Ef-
fective
height
of stack

K: value
deter-
mined
by res-
pective
region





NOX
250ppm at
02=12%




Only for
those
plants
newly
structed
on June
18 1977
and after

Exhuast
gas;
40 000
Nm3/h or
higher
larger

HC1
700mg/Nm3
or lower at
02=12%



Convertion
of concen-
tration;
430ppm or
lower

Applied on
Dec. 1, 1979
and after
for existing
plant, on
June 18 1979
and after
for newly
constructed
plant
                             -  3  -

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                                                               95
      The dust as well as the SOX has been regulated since the
 first enactment of the Air Pollution Control law.   As to NOX
 and HC1, on the other hand,  the regulation has been added to
 the provision of the Law at the revision of July 1977.
      The dust discharge differs according to the type  of
 the incinerator,  the combustion conditions, the quality of the
 wastes and  so on.   However,  in case  of  a continuous incinera-
 tion plant,  the standard levels may  be  fully safisfied  by in-
 stalling the  electrostatic precipitator.
      SOX is  generated by the combustion of sulphur included in
 the waste and the  auxiliary  fuel.  However, the amount  of sul-
 phur included in the wastes  is as  small as 0.04%.   Also,  it is
 becoming a  rare case to use  an auxiliary  fuel for  supporting
 the combustion as  the calories of  the wastes is getting higher.
 So,  any  of  th'e above puts  no serious  problem.   The standard
 value  of SOX  control is determined at each stack hights in such
 a way  that  the maximum concentration  on the ground is controlled
 to  a value lower  than a certain level (As  to Yokohama,  the level
 enacted  at present  is 0.002ppm after  several revisions  of the
 control  to the severer direction).
     NOX is generated by the combustion of nitrogen in  the wastes
 and  the  reaction of  the nigrogen in the combustion air  at a high
 temperature.   Generally the  former is called the Fuel NOX and
 the  latter is  called the Thermal NOX.   In  case  of  a waste in-
 cineration plant, it  is  generally assumed  that  both types of  the
 NOx  are  contributed.   Therefore, the  generation of  NOX  is sup-
 pressed  lower  than the  standard value (250ppm)  by  operating  the
 combustion with minimum volume of excess air or by  the  combus-
 tion control at the  furnace  inside temperature  of  900 to  950°C
 or lower.
     HC1  is generated by the burning of chlorine included in
 the waste plastics, or  the PVC in particular, and other com-
bustiblo  clilorine.  The standard level  of  control  is 700r.:g/"m3
or 430ppm in volume.  This value was determined  by setting  the

-------
                                                             96
target value of the environmental concentration of HC1 to be
0.02ppm, and the exhaust HC1 from incinerators with the stacks
of average height can satisfy it        even at a disadvanta-
geous condition of diffusion.
     By a normal waste incinerator,          the concen-
tration of exhaust HCI may surpass this value in many times.
     At present, therefore, the countermeasure for removing HCI
is one of the most important problems of the incineration fur-
naces in Japan.  In particular, it is an urgent requirement to
investigate the technology which can well suit to the existing
incineration furnaces.
                            - 5 -

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                                                               97
3.   Present status of HC1 from refuse incinerator

  3-1.   Present status of HC1 discharge according to  the
        qualities of  refuse

            The city of Yokohama collects  the household refuse
        including glass bottles,  cans  and other incombustibles
        as well as plastics in a  single  collection.  The average
        composition of the wastes collected by the administra-
        tion is shown in Fig. 2 and Table 2.
                        l,542kcal/kg/^arbage 5.252
                              Shells and egg shells
                                    0.53%
Fig. 2  Composition of collected wastes    Average in 1977  (Yokohama)
                            -  6  -

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                                                       98
   Table 2.  Chemical analysis of as-collected wastes
                            Average in 1977  (Yokohama)
Apparent
speci-
fic
gjravity
0.240
Mois-
ture
content
(%)
49.99
Com-
busti-
bles
(%)
35.72
Elements
included in combustibles (%)
C
19.41
H
2.71
N
0.44
S
0.04
Cl
0.29
0
12.83
Ash
content
(%)
14.29
Low Cal-
orific
value
(kcal/kg)
1542
     The concentration of HC1 in an exhaust gas through
continuous type incinerator with boilers was 456 to 831ppm,
and the average value was 619ppm (Average of 1977, con-
version of 12%02).
     The ratio of plastics in the waste of Yokohama is
increasing as shown in Fig. 3, and 6.04% is reached at
present (1977).

-------

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                                                        100
3-2.   Present status  of HC1  discharge  according  to  the  types
      of refuse incinerators

           The actual status of  the  incinerator  of  continuous
      combustion type with boilers were  discussed in  the pre-
      ceding section  3.1.  The present status  of HC1  discharge
      in the exhaust  gas of  continuous combustion type  inciner-
      ator with water atomizing  gas cooling  chamber  is  as  follows.
           In Yokohama,  where the mixed  collection  of plastics
      is executed,  the rate  of HC1 discharge is  381 to  567ppm,
      or 503ppm on  the average,  while  the rate is 110 to 340ppm,
      or 205ppm on  the average,  in a certain city where the
      wastes are collected by separating the plastics.
           As you see by these examples, the concentration of
      discharged HC1  is  lower at an  incinerator  of  water atom-
      izing type than at an incinerator  with boilers against any
      type of the waste.  This fact  belongs to  the phenomenon
      that HC1 has  a  easily  soluble  property in  water.
           The HC1  discharge can always  be  held  lower than
      the standard  only  when plastic removed waste  is treated
      in an incinerator  with water atomizing chamber.   On the
      other hand, in  the plants  of relatively larger  capacities,
      the treatments  of  such waste are relatively small in
      number.   So,  most  of the incineration plants  of larger
      capacity require a particular  measure for  removing HC1.
                          - 9 -

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                                                                101
4. .General description of the technology for removing HC1  from
    refuse incineration plant

         On the technology for removing HC1 from the  exhaust  gas
    of waste incinerator,  the gas scrubbing by alkaline solution
    is a popular and excellent technique, and may remove such
    high percentage of HC1 as more than 90%.   Such equipment,
    on the other hand, requires a very high costs for construc-
    tion, maintenance and  operation.   In addition,  there are
    also problems as the corrosion of the equipment,  the effect
    inflicted  on the treatment of discharged water, and the
    generation of white smoke by the  increased moisture content
    of the exhaust gas after the scrubbing process.   In addition
    to these disadvantages,  there may also arise in many cases
    the problem of dificulty of acquiring the area for the  equip-
    ment when  such equipment is to be added to an existing  in-
    cineration plant.
         Therefore,  the concentrations of exhaust HC1 show  a
    considerable fluctuation according to the qualities of  the
    waste or the types of  incineration plants.   Even  in case  of
    a waste including plastics,  the concentration of  HC1 discharg-
    ed from an incineration of the waste  ranges
    600 to 700ppm on the average.   So,  a rate of removal as much
    as 40% or  more can satisfies HC1  level under the  standard of
    430ppm.  Therefore,  an investigation of a technique of  re-
    moving HC1 without the problems of the alkaline solution  scrub-
    bing system has  been performed by expecting  not so  high rate
    of removal.   This  case,  in particular,  is  promoted  in such
    a way that a large scale remodelling will  be unnecessary  to
    the existing incineration  plants  which will  be newly brought
    under control  of  the provisions in December  1979.
         The brief description of  the HC1  removing techniques is
    as follows.
                           - 10 -

-------
                                                                       102
       (1)  Wet type 	 The method of removing HC1 in liquid state
                          with the reaction of water or an alkaline
                          solution.
       (2)  Dry type 	 The method of removing HC1 in solid state
                          by the reaction of alkaline solution or
                          alkaline powder.
           A further classification can also be possible into the
      simplified type and the perfect type according to the removal
      rate of HC1.
           There are those at resent under development: or under
      experimentation.  However, they are also in a list below.
      The flow diagrams of each are shown in Fig. 4.
I.  Wet type
             1. Simplified type
             2. Perfect type
 (1)  The  method  of temperature
     reducing by water atomizing
 (2)  Simplified  scrubbing method
 (1)  Perfect  scrubbing method by
     alkali
            ,1. Simplified type
II.  Dry type
             2. Perfect type
 (1) Method  of  alkali  atomizing
    inside  the  incineration
    furnace
 (1) Alkaline solution atomizing
    method
,(2) Moving  bed  system
                              - 11 -

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                                                                   103
From gas
mixing
chamber

To waste
water
treatment


»



(
1



J
*
I

r
i

j
£
	 -to
To Eel

i
r 1
y

r
              From EP
4


r*
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t

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r ~


                                                              To stack
           Gas
                     Gas
                     scrubbing
                     chamber
           scrubbing
           chamber   Supplied  Atomizing
                       City
                       water
                       supply
                                Scrubbing
                                water tank
Type I-l-(l)
by city
supply
water
                                water tank
Type I-l-(2)
                  To waste water
                  treatment
EP


~~& &
\ '
Quick

s^stem^ £_
i '
Scrubbine
NaOH
1
[system

Steam <
1
Dr
!
Reheatinc
kerosene
(system



(
       Type  I-2-(l)
                          Water
                          discharge
                 Water
                 discharge
         Reaction  and evapo-
         ration chamber
                  Cyclone

                  Reaction
                  product
                                           To  stack
                                                                •S   ^-—^
                                                       IndustrialL^_!—i2       E-
                                 water
                     Pump
                                                           Type II-2-(2)
                          Compressed
                          air
        Type  II-2-(l)
                Fig. k  Flow charts  of  representative
                        HC1 removing technologies
                                 -  12 -

-------
                                                              104
5.  Measures for removing HC1 and their efficiencies

         On the policy of Yokohama City, we will continue to exe-
    cute the incineration of collected waste from househoulds
    without separating the plastics.   With this policy in mind,
    the investigation was carried out at the actual incineration
    plants for the countermeasure of  suppressing the HC1 from the
    existing incinerators to under the standard value of 430 ppm.
         As described above, the perfect alkaline scrubbing method
    of wet typ_e (Type 1-2-(1))  is a very excellent technique.
    At the existing incineration plants, however, this has a dif-
    ficult point on the required area and the waste water treat-
    ment. .So, the investigations were executed on the simplified
    scrubbing method of wet type (Type I-l-(2)) (See Figure 5),
    the method of alkali atomization  inside the incineration fur-
    nace (Type II-l-(l)), and the method of the dry type alkaline
    solution atomization (Type  II-2-(l)).

  5-1.  HC1 removing efficiency in the wet type simplified scrubbing
        method
             The wet type simplified scrubbing system has been
        installed between the induced draft fan and the stack by
        Yokohama City before the regulation of HC1 was enforced.
                                                              Q
                      VI
~-~
V t
h-
l-» ,
^
^
, 1
Wet typo si
                   Fig.5   Section View of Plant M
                            - 13 -

-------
                                                           105
      In  this  system,  the  gas  temperature at the inlet
 and  at the  outlet  are designed  to be about  250°C and
 200°C respectively.   These  values are determined to  hold
 the  outlet  temperature of the stack at 180  to  200°C  which
 gives a  favorable  condition to  the atmospheric diffusion
 of the exhaust  gas.   In this case,  gas at relatively high
 temperature is  processed  by scrubbing,  resulting in  the
 lower removal efficiency.   But  this  scrubbing  efficiency
 will be  sufficient if it  is higher than 40%.
      Following  are the brief description of the investi-
 gation result.
      NaOH was added to the  scrubbing solution  so that  the
 alkalinity was  obtained.  However, we could not observe
 any  difference  of  the  removing  function between the  pH
 values of 7,  9  and 11.  Rather, it was  found that the
 efficiency of removal  was controlled by the ratio between
 the volume of the scrubbing solution and that  of  the ex-
 haust gas (L/G  = Scrubbing  solution  ^/Exhaust  gas Nm3).
     Figure 6 shows the relations between the  rate of  HC1
 removal,  the ratio L/G, and    the  temperature drops
 between  the outlet and  inlet of the  scrubbing  equipment.
 Figures  7 and 8 show  the linearized  forms of these trends.
As you see in the figures,  the larger  the value  of L/G,
 the larger the rate of HC1  removal,  accompanied with the
 increasing temperature drop.

-------
                                                                106
 o
 g
 QJ
O
   90


   80


   70


   60


   50


   40


   30
o
01
.u
<2   20
                                                      *   I  Plant
                                                      A   A  Plant
I
10
0
1.0
yf
\\ ' ' '
40 50 60


                                                      •   K Plant
                                                      o   M Plant
2  0.5
o
                            Temperature  drop  at  the  outlet  and  inlet  of
                            simplified scrubbing device  (°C)
              X0
           40     50     60    70     80     90   100    110   120  130
    Fig.  6   Relation  between  the  temperature  drop  at  the outlet  and
            inlet  and the  L/G ratio  as  well  as  the rate of HC1 removal
                              -  15  -

-------
o
-t
ts
o
=
V-

wJ
«/
*•
U>
0
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U-l O
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a 
xX w
2 ^100
x 3 ec
x u C
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x ' B v-
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-------
                                                              108
           At the incineration plant which burns refuse after
      classifying and removing the plastics, the concentration
      of HC1 may be below the controlled value.  In case of
      Yokohama City, however, this method cannot be a perfect
      one because the wastes are burnt mixed with the plastics.

5-2.  HC1 removal efficiency of the method of atomizing alkaline
      into the incineration furnace

           With the aim of removing HC1 at the existing incinera-
      tion furnace with boilers without remodelling the operating
      system in a large scale, the investigation was carried out
      for about two months at two incineration plants on the meth-
      ods of injecting alkaline matters such as Ca(OH)2 or CaCOs
      in powder or slurry into the incineration furnace or a part
      of the flue.  The product (CaCl2> generated by reaction
      with HC1 was collected by the existing electrostatic pre-
      cipitator.
           The investigation results are described as follows:

           The alkaline chemicals were atomized in the plant A at
      the four points shown in Fig. 9.
                          - 17 -

-------
                                                         109
 Fig.  9  Furnace Section View of Plant A

     The points A, B, and C are located at high temperature
zone where the reaction time is relatively long (500 to
900°C, 10 sec or so), and the point D is located at low
temperature zone where the reaction time is short (260 to
300°C, 2 sec or so).
     The relation between the location of atomization and
the ratio of HC1 removal is shown in Fig. 10, and the rela-
tion between the volume of atomized chemical and the ratio
of HC1 removal is shown in Fig. 11.
                    - 18 -

-------
                                                                 110
  100
   80
rt
i  60
o
*  40
o

*•


:
o
A ^
o


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?r >
0 •
o




A

Symbols
A
A
©
O
•
2

Types of
chemicals
CaCOa Powder
CaC03 Slurry
Ca(OH)2 Pox^der j
Ca(OH)z Slurry )
A






            Ratio of atomized equivalents
  Fig. 11  Relation between amount of atomized  chemical  and
           rate of HC1 removal
                               -  19  -

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                                                             111
      Ca(OH)2  showed a higher rate of HC1 removal than CaCOa
 It was also found that a higher rate of removal was ob-
 tained by the powder injection than the slurry injection.
 As to Ca(OH)2,  no difference of the rate of removal was
 observed between the high temperature zone and the low
 temperature zone.   In case of CaCOa, however,  lower rate
 of removal was  observed at the low temperature zone.   As
 to the amount of the chemicals to be injected, the rate
 of removal reached practically a. constant rate at three
 times the equivalent of the amount of the alkaline chemi-
 cal to the generated HC1.
      On the locations of atomization,  when an  alkaline
 chemical of calcium type is atomized at the high tempera-
 ture  zpne,  it is anticipated that the calcium  may deposit
 on the refractory  bricks and the castables inside the
 furnace,  and  the water tubes of the boiler may be blocked.
 So,  the optimum method would be the injection  of Ca(OH)z
 powder into the low temperature zone.
      Based upon the above  discussion,  continuous tests
 were  executed many  times under optimum conditions.  An  ex-
 ample of  such tests  is:   the average concentration of
 generated  HC1 during 90 minutes was 731ppm,  and the average
 HC1 exhaust was  289ppm.  The  rate  of HC1  removal was about
 60% and  the amount  of  injected chemical was  double of  the
 equivalent.
      Therefore,  the method  of  atomizing alkaline matters
 into  the incineration  furnace  was  found to have  a superior
 removing effect  of HC1 with  a  simple operation.   The elec-
 trostatic precipitator  is under  a  higher  load.   From our
 investigation, significant drop  of  the dust  collection
efficiency was not observed at  the electrostatic  precipi-
 tator although the load was increased.  However,  the dust
density in the gas increased at  the  outlet of  the dust
collector.  It is necessary to  investigate the effect on
the dust collector for a longer period.
                   - 20 -

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                                                           112
           However, at an incinerator where the plastics are
      separated from the wastes, the generated HC1 concentration
      is lower than that fron the incineration wastes mixed with
      plastics.  Therefore, a smaller amount of alkaline powder
      is required to be injected with the less effect to the  dust
      collector.

5-3.  HCl removing efficiency of the dry type alkaline solution
      atomizing system

           The method of atomizing alkaline chemical into the
      incineration furnace was discussed in the section 5-2, and
      the rate of HCl removal was 40 to 60%.  When the concentra-
      tion of generated HCl is increased in the future,  or in
      case a higher rate of removal is required,  it becomes
      necessary to increase the rate of removal.   So, the inves-
      tigation of the HCl removal by the dry type alkaline solu-
      tion atomizing method is under way by connecting the test
      equipment to an actual incinerator.
           This method corresponds with the Type  TI-2-(l) of the
      HCl removing techniques.  The Ca(OH)z  slurry is introduced
      into the evaporation chamber to mix with the exhaust gas
      so that the reaction is carried out and produced CaCls  is
      removed by an existing or an independently  installed dust
      collector.  This method also belongs to the dry type as the
      method of the injection system of alkali inside the inciner-
      ation furnace.   So,  there is no influence on the waste water
      treatment.  It  has an excellent advantage of treating the
      exhaust gas as  it is at 260 to 300°C.
           The investigation is still under way,  and a part of
      the obtained results is as follows:
           The passing time (reaction time)  of the gas inside the
      evaporation chamber is designed to be 5 to  7 sec.   The
      amount of Ca(OH>2  to be injected is 1.5 times as the HCl
                          -  21  -

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                                                     113
equivalent at the inlet.  The rate of HC1 removal ob-
tained in this test was 80%.
     In this system a higher rate of removal is obtained
by a smaller volume of chemical with only a small tempe-
rature drop of the exhaust gas.  The CaCla produced is
collected by a followed cyclone before introducing the gas
to an existing dust collector.   So,  only a slight effect
is caused on the existing dust  collector.
                   - 22 -

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6.  Evaluation and conclusion

         For the purpose of coping with the provisions controlling
    the HC1 exhaust, investigations,  although for only a short dura-
    tion,  were executed on each of the techniques of HC1 removal
    suitable for the existing incineration plants using actually
    operated plants.
        As the results, it is judged  that the dry type alkaline
    solution atomizing method (Type II-2-(l)) is the most suitable
    for the incineration plants operated by Yokohama City admini-
    stration where the wastes are collected mixed with the plastics.
    The project of constructing the equipment of this type is being
    promoted" for the operation on the actual basis coping with the
    provisons -controlling the HC1 exhaust to be enforced in December
    1979.
        On the other hand,  CaCIz  produced by the reaction with Ca(OH)2
    is recovered in the form of powder with small value of specific
    gravity.   So,  it becomes necessary to execute a suitable treat-
    ment of the powder.  Relating to  this point, however, an inde-
    pendent study  is under way.  The  method is related to the soli-
    dification of  the flyash recovered by the electrostatic precipi-
    tator  with the aid of the waste plastics, where the volume
    reduction and  the prevention of noxious matters dissolution
    could  be  possible.
                            - 23 -

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                                                              115
                  HCL Removal in Incinerator Plants
             Discussion Leader: Mr. Takashi Miyonohara

Question:  What type of "legal control is being enforced against the
           disposal by incineration"?

Answer:    The answer to the first question can fee found in my report,
           but I would like to answer anyway.  There is a law called the
           Air Pollution Control Law; for water, there is a law called
           the Water Pollution Control Law; and for our incinerators there
           is a law called the Solid Waste Treatment Law.
Question:  Only part of the HCL comes from the plastic in the waste. Where
           does the majority come from?
Answer:    Chlorides, according to our survey, come from plastic, garbage
           and paper waste.  The plastic will be contained in the form of
           polyvinylchloride; garbage will be contained in the form of
           sodium chloride; paper waste will be contained in the form
           of natural salt.  It is hard to say which source contains the
           most chlorides,  however, I suspect that plastics contain
           the most at the source.  I would also like to point out that
           even though those chlorides contained in paper might not be
           much as an absolute figure, as a cumulative total it cannot
           be ignored.  The table we have to explain the chloride sources
           is not specific as to type of sources; however,  we have those
           figures if you would like to have them.

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                                                               116
Question:  What types of metals were used in the scrubbers?  And what




           construction material was best for scrubbers?




Answer:    In the case of the wet type, corrosion would be the major problem.




           Titanium or a type of ceramic would also be satisfactory; in the




           area of low temperatures, we use rubber or plastic-type linings.








Question:  Did anything work?




Answer:    Since we started this research there has -not been enough time




           to determine, i'f anything works; .so, we cannot say at this point




           in time.  I can say that the wet type has to be wet all the




           time; and the dry type has to be kept dry all the time,




Question:  What is the cost of HCL scrubbing?




Answer:    We haven't come up with a figure yet.  However, we expect 20




           pecent higher costs for the wet type.




Question:  There are only two countries in the world that have standards




           for HCL—Germany and Japan.  We wonder what the thinking was



           in Japan for coming out with an HCL standard?




Answer:    It is a very difficult question to answer.  So far we have




           tried to regulate hydrochlori'de gas in industrial facilities.




           So this is an area in which we are now trying to focus our




           effo rts.

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                                                         117
   Guidelines For The Landfill Disposal of Solid Waste



                   Truett DeGeare, Jr.



               Office of Solid Waste, EPA








     The following paper is excerpted from the U.S.-EPA



Guidelines for Landfill Disposal of Solid Waste to be published



in the Federal Register in February 1979.  Public comments



will be solicitated throughout the nation prior to publishing



the final guidelines.  We welcome any comments and discussion



by the Japanese government on the scope, definitions, and



technical aspects of the proposed rules.




I t 241.100 Scope



     (a)  These Guidelines are generally applicable to the



landfill disposal of all solid waste.  Additional guidance



for landfill disposal of solid waste is contained in technical



bulletins which ar e published periodically.  Such technical



bulletins available from the EPA/ Office of Solid Waste,



provide in-depth discussions of disposal of specific solid



wastes by particular technologies.



     (b)  These Guidelines describe environmentally acceptable



landfill disposal operations and present "recommended



practices." These procedures are not meant to be exclusive



or to discourage or preclude the development or use of




equally effective and economical technologies.  It is the




responsibility of a facility's owner or operator to demonstrate



to the responsible agency that techniques other than those



appearing in these Guidelines can provide effective enviro ..".ental



protection.

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                                                            118


 5 241.101 Definitions



     As used in these Guidelines:



     (a)   "Aquifer" moans a geologic formation, group of



formtions,  or part of a formation that is capable of yield-



ing usable quantities of ground water to wells or springs.



     (b)   "Attenuation" means any decrease in the maximum



concentration or total quantity of an applied chemical or



biological constitutent in a fixed time or distance traveled



resulting from physical, chemical and/or biological reaction



or transformation.



     (c)   "Base flood" means a flood that has a 1 percent



or greater chance of recurring in any year or a flood of a



magni-^de equalled or exceeded once in 100 years on the



average over-, a significantly long period.  In any given



lOO-y^sr interval such a flood may not occur, or more than



one such flood may occur.



     (d)   "Cell" means the daily volume of solid wastes that



are deposited and enclosed by cover material in a landfill



disposal facility.


     (e)   "Contamination" means the degredation of naturally


occuring water, air or soil quality either directly or



ii. IJroctly as a result of man's activities.



     (f)   "Contingency Plan" means an organized, planned,



coordinated course of action to be followed in the event



of 3 fire, explosion or discharge or release of waste into



the environment which has the potential for endangering hue?an



health and the environment.
 ">

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                                                       119





      (g)  "Cover material" means soil or other suitable




material that is spread and compacted on the top and side




slopes of disposed solid waste in orde1" to:  control vectors,




gases, erosion, fires, and infiltration of precipitation;




support vegetation; provide trafficability; or assure an




aesthetic appearance.




      (h)  "Disposal" means the discharge, deposit, injection,




dumping, spilling, leaking, or placing of any solid waste or




hazardous waste into or on any land or water so that such



solid waste or hazardous waste or any constituent thereof




may enter the environment or be emitted into the air or



discharged into any waters, including ground waters



      (i)  "Facility structures" means any buildings or other



structures, or utility or drainage lines on the landfill



disposal facility.




      (j)  "Floodplain" means the lowland and relatively flat



areas adjoining inland and coastal waters, including flood-



prone areas of offshore islands, which are inundated by the



base flood.



      (k)  "Ground water" means water below the land surface



in the zone of saturation.



      (1)  "Hazardous waste" means those wastes identified by




list or by characteristic in regulations promulgated pur-




suant to Section 3001 of Pub. L. 94-580.

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                                                       120
     (m)  "Landfill" means a facility for the disposal of



solid waste involving the placement of solid waste on or



into the land surface, and usually involving compaction and



covering of the disposed solid waste, and which is not a



landspreading or surface impoundment facility.



     (n)  "Leachate" means liquid containing dissolved or



suspended materials that emerges from solid waste.



     (o)  "Liner" means a layer of emplaced materials beneath



a landfill which serves to restrict the escape of wastes or



their constituents from the landfill.



     (p)  "Monitoring Well" means a well used to obtain



water samples for water quality analysis or to measure



groundwater levels.



     (q)  "Open burning" means the combustion of solid waste



without (1)  control of combustion air to maintain adequate



temperature for efficient combustion, (2) containment of the



combustion reaction in an enclosed device to provide suffi-



cient residence time and mixing for complete combustion, and



(3) control of the emission of the corobustion products.



     (r)  "Periodic application of cover material" means the



application of soil or other suitable material over disposed



solid waste at such frequencies and in such a manner as to



control vectors and infiltration of precipitation; reduce



and contain odors, fires, and litter; and to enhance the



facility's appearance and future utilization.

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                                                     121
      (s)  "Permafrost" means permanently frozen subsoil.
      (t)  "Plans" means technical reports and engineering
drawings, including a narrative operating description,
prepared by professionals which properly Describe and record
the landfill disposal facility and its proposed operation.
      (u)  "Potential zone of influence" means that area
within a water resource which could be contaminated by
leachate or other materials derived from a landfill disposal
facility.
      (v)  "Recharge zone" means an area through which water
enters an aquifer.
      (w)  "Responsible agency" means any organization that
has the legal duty to ensure that owners, operators or users
of land disposal sites comply with these guidelines or other
applicable regulations.
      (x)  "Runoff" means the portion of precipitation that
drains from an area as surface flow.
      (y)  "Salvaging" means the controlled removal of waste
materials for utilization.
      (z)  "Scavenging" means uncontrolled removal of solid
waste materials.
      (a a) "Sludge" means any solid, smisolid, or liquid
waste generated from a municipal, commercial, or industrial
wastewater treatment plant, water supply treatment plant, or
air pollution control facility or any other such waste
having similar characteristics and effects.

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                                                        122



     (bb) "Sole Source Aquifers" means those aquifers, which



solely or principally supply drinking water to a large




percentage of a populated area.




     (cc) "Solid waste" means any garbage, refuse, sludge



from a waste treatment plant, water supply treatment plant,




or air pollution control facility and other discarded material,



including solid, liquid, semisolid, or contained gaseous



material resulting from industrial, commercial, mining, and



agricultural operations, and from community activies, but




does not include solid or dissolved material in domestic



sewage, or solid or dissolved materials in irrigation return




flows or industrial discharges which are point sources




subject to permits under the Federal Water Pollution Control




Act, or source, special nuclear, or byproduct material as



defined by the Atomic Energy Act of 1954.



     (dd) "State" means any of the several States, the



District of Columbia, the Coroir.onwealth of Puerto Rico, the



Virgin Islands, Guam, American Samoa, and the Northern



Mariana Islands.



     (ee) "Ten-year 24 hour precipitation event" means the



maximum 24 hour precipitation event with a probable re-




occurrence interval of once in 10 years.




     (ff) "Water table" means the upper surface of the zone




of saturation in an unconfined aquifer at which the pressure




is equal to atmospheric pressure.

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                                                         123







     (gg) "Wetlands" means those areas that are inundated or




saturated by surface or groundwater at a frequency and




duration sufficient to support, and that under normal




circumstances do support, a prevalence of vegetation typically




adapted for life in saturated soil condition. Wetlands




generally include swamps, marshes, bogs, and similar areas.

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                                                           124


§ 241.200 Site Selection

g
s 241.200-1 General.  Selection of a site is the most critical


step in establishing a landfill disposal facility.  Site


selection must be accomplished in consideration of:  ground


and surface water conditions; geology, soils and topographic


features; solid waste types and quantities; social, geographic


and economic factors, and aesthetic and environmental impacts.


§ 241.200-2 Recommended Practices.  Site selection should be


accomplished in accordance with the following:


     (a)  Environmentally sensitive areas, including wetlands,


100-year floodplains, permafrost areas, critical habitats of


endangered species, and recharge zones of sole source aquifers


should be avoided or receive lowest priority as potential


locations for landfill disposal facilities.  If these areas


are to be considered the following subjects need to be


addressed:


     (1)  Alternatives.  Before concluding that location of

a landfill in an environmentally sensitive area is advisable,


alternative locations and disposal techniques should be


evaluated in terms of hydrogeologic, technological, environmental,


economic and other pertinent factors.  /Alternatives involving


regional facilities, resource recovery, or both, should also


be considered.  Increased costs, alone, should not be

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                                                      125
sufficient grounds for dismissing an alternative in favor of




disposal in an environmentally sensitive area.




     (2)  Impact.  A comprehensive analysis of location of a




landfill in an environmentally sensitive area should be




performed and provided to the responsible agency or agencies




along with the discussion of alternatives.  Such analyses




should include:  an estimate of the type and extent of




potential impact on the ecosystem; consideration of design,




construction and maintenance techniques to minimize, prevent




or correct such impacts; and a general appraisal of the area




in terms of rate of encroachment, cumulative impact, and




multiplier effect of activities in that area.




     (3)  Approvals.  Before locating a landfill in an




environmentally sensitive area permission must be obtained




under various authorities.




     (b)  Zones of active faults and karst terrain should be




avoided in locating landfill disposal facilities unless a




site-specific evaluation demonstrates nininram potential for



adverse effects, especially upon grour.clwater.




     (c)  If it can be shovn that no other feasible alternative



location exists, a landfill disposal facility may be engineered



for location in a generally unsuitable area.



     (d)  The cost effuctivsness of a site's selection




should be determined, if considered environmentally feasible.




This cost analysis should include act only the economics of




tha disposal facility operation but c;] :>o the impact of the




planned future usa of the site afuor completion of landfill




> ;: orations.



                             9

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                                                       126
      (e)  The possible incorporation of a site into a regional



solid waste disposal system whether currently in existence



or a future possibility, should be considered during environmental



and economic evaluations.



      (f)  Sites traversed by pipes or conduits (for sewage,



storm water, etc.) should be rejected unless their reloca-



tion or protection is feasible.   Since such pipes may serve



as' pathways for gas and leachate extreme caution must be



observed and a plan for pipe maintenance and repair developed.



      (g)  Characteristics and availability of on-site soil



should b* evaluated with respect to their effects on site



performance and site operations, such as, use of the soil as



cover material and its effect on vehicle maneuverability.



      (h)  Sites located in the vicinity of airports, which could



attract birds to the disposal facility should be designed



and operated so as to not pose a hazard to aircraft.



      (i)  Sites should be accessible to appropriate vehicles



by all-weather roads leading front the public road system.



      (j)  The potential socio-economic effects of a site's



selection should be determined.  Topics to be addressed



include aesthetic arid safety considerations such as vehicular



traffic, litter, noise and other possible nuisance conditions.
                             10

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                                                       127
§ 241.201 Design



§ 241.201-1 General.  Sufficient design is essential to the



successful operation of a facility in even the best location.




In the design phase of a landfill disposal facility all the




requirements and technology alternatives to satisfy those




requirements are reviewed prior to incorporation into the



design.  The design involves the evaluation and documentation



of a landfill disposal facility capable of accepting certain



solid waste materials for disposal.



§ 241.201-2 Recommended Practices.  A landfill disposal




facility should be designed in accordance with the following:



     (a)  The types and quantities of all solid waste expected




to be disposed at the landfill should be determined by



survey and analysis to serve as a basis for design.




     (b)  Current and projected use of groundwater resources



in the vicinity of the landfill disposal facility should be



determined as a basis for design of any necessary groundwater



protection and monitoring system as follows:



     (1)  Establish initial (background) quality of water



resources in the potential zone of influence.



     (2)  Establish the depth to the water table and the



direction and rate of groundwater flow with special con-



sideration of current and projected withdrawal rates by



ground waters users.
                             11

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                                                           128
     (3)  Establish potential interactions oc the landfill




disposal facility, its hydrogeology,  and the areal ground and




surface waters, based upon historical records and other



sources of information.




     (4)  Establish site geology, at least down to the



mean annual water table with specific emphasis on hydraulic




conductivity and the possible natural attenuative capacity



of the soils and subsurface geology.




     (c)  Quality, quantity/ source and seasonal variations




of surface waters in the vicinity of the landfill disposal




facility should be established to serve as a basis for




design of any necessary surface water protection and monitoring



system.




     (d)  The nearby floodplain  (defined by the 100 year



flood level) should be established in accordance with pro-



cedures described in "Guidelines for Determining Flood Flow



Frequency", Bulletin No. 17a, Water Resources Council,



Hydrology Committee, June 1977.  If all or part of the



facility lies .within the 100 year floor: plain a suitable



dike to prevent facility inundation should be detailed in




the site design.



      (c)  A water balance for  irhs landfill disposal facility




should  be established  to serve as a basis for design of



leaohate control  and surface runoff systems.  The method
                               12

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                                                      129





co:. Lai nod in "tJse of the Water Balance Method for Predicting




Loach-ate Generation from Solid Waste Disposal Sites1'  (Si\-




Io2)  is an example of a technique for accomplishing this.




      (f)  Landfill leachate generation cannot be avoided




ex'j cot in some arid climates, therefore, leachate control




measures for water quality protection should be incorporated




in the site design, as required,  (re:  Section 241.202).




      (g)  Since most organic waste material undergoes decom-




position in a landfill, decomposition gas will be generated.




The landfill design should include measures for control of




these and other potential gaseous emissions, as required,




(re:   Section 241.203).




      (h)  The final design of a landfill disposal facility




can cr.Ly be accomplished after a thorough analysis of tradeoffs




among environment a. 1 impacts, economic considerations, future




use alternatives and nature and quantities of the waste to




bo disposed has been accomplished.  This tradeoff analysis




cannot be overemphasized in light of potentially conflicting




landfill control technologies.  For example, minimization of




lenchate generation can be accomplished, in part, by sealing




the surface of a landfill, hsv/ever, the surface seal will




effectively minimize escape of decomposition gases from the




landfill which may result in potentially dangerous off-site




gas migration.   Selection of control technologies, therefore,
                             13

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                                                      130
ir.u:-. L consider Lho impact of companion  technologies  at a.

landril] disposal facility and be compatible v/.ith  the planned

end us'.j of the site.

     (i)  Plans for design, construction, operation and main-

tenance of new sites or ir.odifications  to existing  sites

sh ouId include:

     (1)  Evidence of compliance with  applicable  "Criteria

for Classification of Solid Waste Disposal facilities" (40

CFR 257).

     (2)  Demonstrated consistency with the  "Recommended

Practices" of these guidelines, or suitable alternative

technologies.

     (3)  Careful detailing of all design and operational

considerations necessary to bring site conditions  to an

acceptable level.

     (4)  A  clear presentation and discussion of any separate

areas which  have bean incorporated into the landfill design

for disposal of specific wastes requiring special  or separate

handling.

     (5)  Other pertinent information, such as:

     (i)  Initial and final topographies at contour intervals

of 5 feet or less as specified by the  appropriate  regulatory

authority.

     (ii) Land use and zoning within,  at least, one-quarter

mile of  th.'-i  site showing true location  of all residences,

buildings, public and private wells, water courses, rock

outcroppings, roads.

      (iii) Location of all airports within two  (2)  nile:--.

of tho  £-.ite.

                               14

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                                                         131





     (iv)  Location o£ all utilities v/ithin, at  Ie£i3t,  500




feet of the site.



     (v)  Temporary anJ permanent all weather access  roiids.




     (vi)  Screening and other nuisance control  rnonsure:;.




     (vii) Site monitoring locations.




     (viii) Sedimentation control plans.




     (ix)  Narrative descriptions, with associated  technical



drawings,  indicating site development and operation procedures,




     (x)  Contingency plans.




     (xi)  Projected use of completed site.




     (xii) Long term maintenance procedures.
                              15

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                                                        132
g 241.202 Leachate Control




§ 241.202-1 General.  Entry of landfill leachate into ground



or surface water may result in an adverse impact upon those



waters. Landfill leachate management techniques include




control of leachate production, control of escape of leachate




from a landfill and control of the impact of leachate on




the environment.  Application of one or more of these



techniques at a landfill will be a function of the degree of




protection of ground and surface water necessary at the



specific site of a landfill disposal fadility.  There are



two extreme approaches to landfi.M leachate management;.  One




extreme involves complete reliance upon attenuation capabilities




of the natural hydrogeologic system which incorporates



biological, chemical and physical systems, including dilution,



to abate the impact of leachate on ground and surface water.



This approach requires a full understanding of the subsurface



conditions at a landfill disposal site from the natural



ground surface, at least, to the bottom of the upper most



saturated zone and a soundly based estimate of the anticipated




landfill leachate quality and rate of generation.  Analysis



must show that the attenuation capability of soils in the



unsaturated zone and dilution capacity of the saturated zone



are sufficient to maintain the required ground and surface



water quality for this approach to be utilized.  The other
                             16

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                                                       133




cxtfjipx-i involves the maximum containment oC landfill leachate




by vrrious techniques.  In accordance v;ith Section  241.201,



either approach requires a case-by-case evaluation.    Since




those approaches are the extremes/ actual practice  at  a




specific site will usually require a leachate maucige:Ment




approach somewhere in betv/een.




§ 241.202-2 Recommended Practices.  Leachate control,  when




necessary in accordance with site design, should be accom-




plished 'through application of one or more of the following




practices :




      (a)  Unless underlying groundwater is determined  to be




unusable as a drinking water or other supply source and




therefore not in need of protection, the bottom of  a landfill



disposal facility should be substantially  (1.5 meters  or more)




above the seasonal high groundwater table,, to prevent  direct



contacr of disposed solid waste and the groundwater.   Depending




upon the site design and degree of groundwater protection




required, the unsaturated zone, between the water table and



landfill bottom, can be equipped with monitoring devices to



monitor the passage of leachate, if any, through this  zone;



or, relied upon to provide, at least, minimal attenuation of



planned or unplanned escape of landfill leachate.   In  high



groundwater table areas it may be necessary to lower the



water table.




      (b)  Since the flow of surface water on a landfill can



result in cover soil and solid waste erosion, as well  an
                              17

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                                                          134






i ncroa';-:d loachnte generation, there should be no uneo.itrollod




hydraulic connection between the landfill and si; and ing or




f Lov.'iiVj 'surface water.




     (1)  Surface runoff diversion structures should be con-




structed surrounding the landfill capable of diverting away




from the landfill all of the surface water runoff from tho




upland drainage area from the 10 year 24 hour precipitation




event.




     (2)  A dike with sufficient structural integrity,




should be constructed around any landfill disposal facility




lodated within the 100-year floodplain of sufficient height




to prevent inundation. . Subsurface controls may also be




necessary to prevent intrusion of water resulting from the




temporary elevated. groundwater table, during flooding.




     (c)  Similar to surface runoff from surrounding areas,




incident precipitation  (e.g. rain or snow) falling onto a




landfill can result in two effects, nar.ely, increased




leachate generation and erosion cf cover soil and solid




waste.   Techniques to carry incident precipitation from the




landfill without causing erosion should be applied, as




follows:




     (1)  The final cover of the landfill should be graded




such that water does not pool cv?r th^ landfill.  In order




to minimize soil erosion the final grade should not exceed




30''.;.  SJopes longer than 7.5 motors (25 feat) may require
                               18

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                                                          135





ci'.tdi tional erosion control measures, such  as, construction




of horizontal terraces, of sufficient width  for equipment




operation, for each 6 meters  (20 feet) rise  in elevation.




Mir.iraum slope, including terraces, should  bo ?.%.




     (2)  The final soil cover on a completed landfill  disposal




facility should be seeded or otherwise vegetated to  minimize




erosion and maximize evapotranspiration.




     (3)  The cover material should be selected to achieve




the i^ajor functions of:



     (i)  trafficability



     (ii) water infiltration control



     (iii) gas migration control




     (iv) fire resistance




     (v)  erosion control




     (vi) vector control



     (vii) support of vegetation




     (4)  If landfill site design incorporates minimization



of Icachate generation a low permeability  cover soil with a



low swell and shrink tendency upon wetting and drying should



be utilized to avoid cracking.



     (5)  If landfill site design allows infiltration of




incident precipitation or re-circulation of leachate  to



encourage waste stabilization a suitably high parmeeibility



cover soil should be utilized to avojLci ponding.
                             19

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                                                       136




     (d)  The design of all landfill disposal faciliLies  should




bn accomplished only after careful consideration of site




hyirogeologic conditions which are to be relied upon, in  part,




f.o : minimization of the impact of the anticipated quantity and




quality of landfill leachate upon ground and surface water.




These considerations include an estimate of the attenuation




capabilities of site soils and the quantity and quality of




ground and surface water.  The degree of reliance upon natural




site hydrogeologic conditions depends upon the degree of




protection required for underlying groundwater.  Protection




of an underground water supply aquifer can be accomplished




as follows:




     (1)  Where natural hydrogeologic conditions are




sufficient to ameliorate the ir.pact of leachate upon under-




lying groundwater no bottom control, beyond naturally




occurring soil layers, is necessary.  Control of infiltra-




ting incident precipitation through selection and placement




of low permeability cover soil can reduce the total quantity




of leachate which will enter the groundwater.




     (2)  Where natural rydrogeologic conditions are unable




to ameliorate the impact of the total quantity of leachate




 (as it  is formed) upon underlying groundwater, the bottom




 (and sides below natural grade) of the landfill should be




lined with loxv perr.eab.ilit/ yoil or other suitable material.




The function of liner material is threefold:  to delay the
                                20

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                                                          137





03-_.ar.e o£  leachato  Crora th.-_> bottom of:  the liner Tor a period




of  time  equal  to  the  liner permeability multiplied by the




thickno3d  of the  liner;  to control the rate of escape of




le.v-'hate from  the bottom of the liner  which must then be




a.r-jlioratecl by attenuation or dilution by underlying soils




•or  ground-water; and to  provide some degree of attenuation as




leachate passes through the liner material.  The quantity of




leachate which must be  handled by the  liner can be minimized




through  selection and placement of low permeability cover




soil to  reduce the  infiltration of incident precipitation.




      (3)   fthere natural hydrogeologic  conditions can provide




only minimal amelioration of the impact of leachate upon




underlying groundwater  it is necessary to minimize the




amount: of  leachate  which is given the  opportunity to enter




the underlying soils  by constantly removing, by drainage,




the leachate which  is intercepted by the liner material.  This




may be coupled with minimization of infiltrating incident




precipitation  by  selection and placement of low permeability




cover soil.




      (4)   Where natural hydrogeologic  conditions are virtually




incapable  of ameliorating the impact oc any leachate upon




underlying groundv;ater  and the underlying groundwater is




particularly valuable it is necessary  to preclude the




escape of  leachate  from the bot'c:o:r. of  th-:-> landfill through




placemen.;:  of multiple liners and constant drainage systems.
                                21

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                                                          138




Ini  • ',-upLion of: the downward  flow OL  loachate  by placement




of. a slightly permeable liner, designed  for  continuous




rcmov.il of leachate, and underlain by a  significantly less




permeable liner material, also de-signed  for  continuous




removal of; leachate, should preclude  the escape of leachato




from the bottora of the lower-most liner.




     (G)  Many types of material can  function  successfully




a:; liners.  The rate of passage of leachate  through liner




materials is a function of the measured  permeability of the




material and the depth  (or head) of leachate on the liner.




In general, the rate of flow  increases v/ith  depth of leachate.




The variety of liner materials available include:




     (1)  Naturally occurring materials  such as clays.




     (2)  Amended natural materials such as  soil cernents.




     (3)  Artificial materials such as asphaltic materials and




polymeric membranes.




     (f)  Liner materials v;hich are to significantly restrict




the rate of flow of leachate  ficrri the bottom of a landfill




should have the following properties:




     (1)  permeability of ixlC-7 en/sac  (about 0.1 foot/year)




or  less.




     (.2)  resist physical and chemical attack  by leachate.




     (3)  capable of maintaining integrity for the design life




 (which must be? determined on  a site-specific basis).
                               22

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                                                              "139
     (q)  The nin Lv.v.rir, allov/ablc  thickness  for both  natural and



artificial liner materials is determined by  either  the



cU'.jTco of quality control and construction preictice for



liner olaccment, or  the thickness  necessary  to  provide a



suitable structure to achieve the  desired  .volumetric release



of leachate f^r the  maximum  leachate  storaye anticipated,-



in accordance with the approved  landfill design.



     (1)  the practical minimum  thickness  for natural soil liners



is 30 cm  (12 inches) and



     (2)  the practical minimum  thickness  for synthetic membrane



liners is twenty  (20) nils.



     (h)  Artificial liner material,  if selected,  should be placed



upon a carefully prepared base of  selected material which will



prevent liner puncture while providing uniform  support, and should



be covered with suitable material  that will  further protect the



liner frcui damage ana provide a  drainage blanket  for the leachate



collection system.   Approximately  60  cm  (2 feet)  of material



is effective in protecting a liner from mechanical  damage



(puncture).  The  lowest 15 cm  (6 inches) of  martial should



be highly permeable  to allow the leachate  collection system



to function properly.



     (i)  Removal of leachate collected on a liner  should be



incorporated into the design of  a  lined landfill  to avoid surface



seeping and relieve  hydraulic pressure on  the liner.  To



facilitate leachate  removal, liner ir.-nterials should be



sloped  to one or  more points and covered with a layer of



highly  pr.rr^able  natar-in.] such as  pea gravel.   7\  grade of lu



or r.ioj;e should be utilised.

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                                                               140
       (;)   Once collected, landfill leachate  should be disposed

  to the land or surface water in an environmentally sound

  manner to protect surface and ground-water quality.   Leachate

  treatment and disposal should be performed in  accordance

  with the following recommendations:

       (1)   Municipal solid waste landfill  leachates have

  generally been shown to be treatable  by various wastewater

  treatment techniques as follows:

       (i)   Leachate treatability -
     Leachate Quality
Treatment Efficiency"





Age of fill

Young
K5 yr)
Medium
(5 yr-10 yr)
Old
(>10 yr)





COD T'"1'/!

10,000

500-10,000

500








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CHIAi:, E.S.K.  and  F.B.  DoVAL.'l-;.  Sanit-nrry Landfill  I e iic]-\ a r/3 s
an-3 i;h?ir Treatment,   Procc-:;-:j.a;r3 A5CE, Jonnal of the
Environs .ntal  Engineering Division 102, FE2, 411-31.   1976.

-l-(COP roi'oval:   C~good, F-fr;ir, r-p:>or)

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                                                           141





     (ii) Lcachutes containing a significant fraction of




biologically refractory high molecular weight organic compounds



(i.e. those in excess of 50,000) are best treated by physical/




chemical methods such as line addition followed by settling.



     (iii) Leachates containing prinarily low molecular weight



organic compounds are best treated by biological methods such



activated sludge.




     (iv) Leachate treatment by combinations of chemical,




physical and biological methods may be required to achieve




discharge standards.




     (2)  Raw or treated landfill leachate should be dis-



charged into a municipal or industrial wastewater treatment




system, only if this discharge will not result in violation




of an ITPDSS permit for that wastevater treatment system.




Limited experience has shown that when raw municipal solid




waste leachate volume exceeds about 5% of the total waste-



water treatment plant flow, interruption of biological



treatment processes may occur.



     (3)  Raxv or treated leachate can be disposed by



controlled application onto the surface of the land provided



sufficient acreage is available and hydrology, soil type,



veger.arion, topography and climate for leachate disposal



have been considered and surface or groundwater contami-




nation will not occur, in violation of the "Criteria for




Classification of Solid Uastc Disposal Facilities" (40 CFR



257).
                             25

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                                                           142






     (•')  ^circulation of collected landfill leachate onto




active or completed sections of the landfill can reduce




leuch'Vcc constituent concentrations by chemical, physical



and biological processes and may be effective in reducing



leachate volume.  This technique can result in, at least,




partial stabilization of young  (0-5 years) landfill leachates




which are relatively concentrated in comparison with rather




old stabilized landfill leachates.
                             26

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                                                             143
p, 2 •; 1.2 o
s 241.203-1 General.  Control of gases from a landfill
die-.posal facility may be . accomplished, by techniques which:
rr.inii.iize the production of decomposition gases or occurrence
of other harmful gases; control the escape of gases into  the
atmosphere; and minimize the migration of gases into soils
surrounding the site.
§ 2-11.203-2 Recommended Practices.  Gas control should be
accomplished in accordance with the following:
      (a)  Leachate and runoff control measures which are
intended to minimize the infiltration of water into a solid
waste landfill may also serve to reduce the rate of gas
generation, primarily CH^ and CO , resulting from decomposition
of disposed organic solid waste.
      (b.)  Volatile solid waste materials or wastes with a
known high potential for release of harmful gases as a result of
chemical reaction should not be accepted for disposal at  a
landfill disposal facility where such gases are required  to be
minimized or avoided.
      (c)  Encapsulation of solid waste in a landfill  (e.g. low
permeability liner and f:i".r.tl cover) to prevent or minimize
infiltrating water should, be coupled with an effective
ver.tils.tion system to prevent the build up of gas pressure
wihhin the landfill, as ncce:;sary.
      (d)  If a relatively porous material is used for cover
at o.  landfill, which does not impede infiltrating water ,
                                27

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                                                             144
ga-je.o shoald nigrdLo vertically out o f the landfill surface,
except when frozen or saturated, for dissipation into the
at ;•:.'_> sphere. However, deep landfills may experience gets
pressure buildup, regardless of cover used.
      (e)  Since horizontal migration of gases from landfills
(duo to both diffusion and pressure gradients) through
surrounding soils is not uncommon an analysis of the land
area surrounding the landfill proper should be performed
utilizing techniques for estimating gas flow through porous
media.  For shallow landfills a "rule of thumb" for estimating
potential gas migration is a distance equal to ten  (10) times
the maximum depth of the landfill below original grade.  If
nearby underground utilities exist, additional examination
along the utility corridor should be performed.
      (f)  Passive barriers which may be considered for the
prevention of horizontal migration of gases include:
      (1)  Cutoff walls constructed of naturally occurring
materials, such as compacted moist clays, or artificial
materials, such as asphaltic or polymeric materials.
      (i)  To assure effectiveness the cutoff wall should
extend  from the ground surface down to a gas impervious layer
(e.g. bedrock or groundwater) below the bottom of the landfill.
      (ii) Even though polymeric materials may be virtually
impermeable to water they should be evaluated for permeability
to qasas.
                                28

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                                                       145






      (iii) Even when compacted, clays and otrhor soils  ore




inpeimenblG to gases only when water saturated.




      (iv) Once in place, properly constructed cutoff walls




should require no maintenance.




      (2)  Venting systems, frequently used in the past,




installed either on or off the landfill proper, consist  of




either gravel filled trenches, perforated pipes, or both.




      (i)  Perforated pipes have been shown to be of limited




effectiveness except in the immediate vicinity of the  pipe




and are therefore not recommended for reduction of pressure




in a landfill, when used alone.




      (ii) Gravel filled trenches, while generally more effec-




tive "than perforated pipes, still permit some migration  of




gases across the trench, especially when covered by snow.or




ice.




      (iii) Gravel filled trenches equipped with vertical




perforated pipes have been shown to reduce the effect  of




temporary covers such as ice or snow but remain of limited




effectiveness in landfill gas migration control.




      (iv) Gravel filled trenches must usually be equipped




for removal of water or leach-ate fro:" tha trench bottom




and are susceptible to plugging by biomass buildup.




      (3)  Combination passive barriers installed off the




landfill, which consist of grc-.vel filled trenches in com-




bination with, an imoermsablo barrier instilled on th.3  side
                              29

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                                                         146




of" the- troach opposite the landfill, provide  good  protection




cK;ain.-;t horizontal gas migration when keyed to  a gas  inper-




:?.::.:'.jle strata bolow the landfill.




      (g)   Active beirriers which may be considered  for tho



prevention of horizontal migration of gases include:




      (1)   Induced exhaust uells, consisting of  several wells




0:1 or off the landfill equipped with perforated pipes connected.



to a pump or blower by a common header pipe.




      (i)   Such systems are very effective when  properly



designed and installed.




      (ii) Such systems are not limited to shallow  landfills




or shallow impermeable substrata.




      iiii) Exhaust gases may be "flared" or recovered.




      (iv)  Such systems nay require significant maintenance.



      (2)   Induced exhaust trenches, consisting  of  surface




sealed gravel filled trenches equipped with perforated



header pipes connected to a purr.p or blower.



      (i)   Such systems are r.ore effective for controlling



gas movement than exhaust walls/ especially at  shallow



landfills, but require more extensive construction.



      (ii) Such systems r.v:.y require significant  maintenance.



      (i.ii) Use with recovery systems is unlikely due  to




introduction of air.



      (3)   Induced recharge trenches are of the  same design



as iT-.duccd exhaust trench:;:; but operate in reverse,
                               30

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                                                          147
sup;icessing horizontal migration  through introduction of




air, under pressure, into the  trench.




     (i)  Such systems have  lov/er power  requirements than




c-;::hri.ust trenches.



     (ii) A gas flare is not necessary since gases are not




concentrated,




     (iii) Such systems rely upon dispersion of gases to *-he




atmosphere across the trench and  ground  surface.
                                 31

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                                                          148
          Ou;^ Contro L
?j 2-' 1.204-1 General.  Control of surface water runoff  at  a




] a'.a :i.ll disposal facility is necessary in order to minimize




th~ potential for environmental damage to ground and surface




waters by direct and indirect effects. Direct surface  water




contamination can result from solid waste and other dissolved




or suspended contaminants carried by surface runoff.




Uncontrolled surface runoff can also contribute to leachate




 (and gas) generation thereby increasing the potential  for both




surface and groundwater contamination.-




§ 241.204-2 Recommended Practices.  Surface water runoff




control should be accomplished at a landfill disposal  facility




in acc-rrciar.ee with the following:




      (a)  Landfill disposal facilities should be located




where the potential for surface drainage onto the landfill




from adjacent land is minimal.
       -j
      (b)  Landfill disposal facilities should be equipped




with suitable channeling devices, such as ditches, berms  or




dikes, to divert surface runoff  from the land area contiguous




to the landfill.




      (c)  Incident precipitation at a land£i11 will  either




evcipora Le, runoff or infiltrate.  To minimize leachate




generation the  final cover on  the landfill  should b?,- graded




to maximize runoff with due concern for erosion.  The landfill






                               32

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                                                      149





sucf.ac" should bo sloped to graders  ion:; than  30?.  to  rna.r.ico




runoff v;ithout causing erosion probl;v.3.  Vegetation of  the




sloped landfill surface will also minimize erosion of cover




soil.




      (d)  Well-comcacted, fine-grained  soils  should  be used




for final cover to enhance runoff while minimizing infiltra-




tion.




      (e)  Runoff not contaminated by solid waste  or  by




leachate from seeps should be routed to a "stilling  basin"




to remove sediment before discharge to  a receiving stream.




Other sedimentation control measures may be equally  effective
                                33

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                                                       150
§ 241.205 Operation



§ 241.205-1 General.  A solid waste landfill disposal facility



should be operated in accordance with the Recommended Practices



of these guidelines or other equivalent practices.



f 241.205-2 Recommended Practices.  A facility for the



landfill disposal of solid waste should be operated in



accordance with the following:



     (a)  In general, only wastes for which the facility has



been specifically designed should be accepted for disposal;



however, other wastes may be accepted if it has been demon-



strated to the responsible agency that they can be satis-



factorily disposed within the design capability or after



appropriate facility modifications.



     (1)  Specific wastes, whose chemical, biological or



physical characteristics are not compatible with the dis-



posal site design, location or operation and which could



pose an unacceptable environmental or health effect or pose



a threat to the safety of personnel or users of the facility,



should be prohibited from acceptance for disposal.



     (2)  In no case may hazardous wastes be accepted for



disposal unless the facility has received a permit for the



disposal of hazardous waste in accordance with regulations



promulgated under Sections 3004 and 3005 of Pub. L. 94-580.
                            34

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                                                        151
      (3)  Facility design features may require prohibition or



pretreatment of certain solid wastes.  For example, unless



the facility incorporates a leachate control system with



sufficient capability to accept liquid or semi-solid wastes,



such receipt may need to be prohibited or materials such as



water treatment sludges may require dewatering before acceptance,



      (b)  Cover material should be applied, if necessary, to



minimize fire hazards, odors, blowing litter, vector food



and harborage; control gas venting and infiltration of pre-



cipitation; discourage scavenging; and provide an aesthetic



appearance.



      (1)  A minimum of 15cm. (6 inches) of soil cover material



sh'ould be applied daily.



      (2)  Cells which will not have additional wastes placed



on them for three months or more should be covered with



30cm. (12 inches) of cover material.



      (3)  Most soil materials can satisfy the purposes of



cover soil.  However, if minimization of infiltration is



necessary, relatively low permeability cover material should



be utilized and placed at the steepest practicable grade in



order to encourage runoff.  Low permeability soils will



remain effective only if the soil has a low shrink-swell



potential or if the soil moisture can be maintained to



prevent cracks from shrinkage and swelling.
                             35

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                                                        152





     (4)  The completed landfill should be covered with 15cm



(6 inches)  of clay or other suitable material with permeability



equal to or less than 1 x 10-7 cm/sec or equivalent, followed



by a minimum cover of 45cm (18 inches)  of additional soil to



complete the final cover and support vegetation.  Deeply



rooted vegetation may require an even greater depth of



suitable soil.



     (c)  In order to conserve landfill disposal site capacity



and preserve land resources solid wastes should be incorporated



into the landfill in the smallest practicable volume.



     (1)  For most solid waste materials landfill compaction



equipment is necessary for volume reduction.



     (2)  Compaction or other volume reduction may take



place at or before delivery to the landfill, by utilizing



balers, shredders, or stationary compactors.



     (3)  Compaction of solid waste ana cover soil reduces



the attraction of rodents and vectors and the potential for



fires.



     (4)  Open burning of solid waste for volume reduction



should not be permitted.



     (d)  The land disposal site should be designed, con-



structed and operated in a manner so as to protect the



health and safety of personnel and users through strict



supervision of operations and site access.
                            36

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                                                     153
      (1)  A safety manual should be available for use by



employees, and they should be instructed in application of



its procedures.



      (2)  Personal safety devices such as hard hats, gloves,




safety glasses, and footwear should be required for facility




employees.



      (3)  Safety devices, including but not limited to such




items as rollover protective structures, seat belts, audible




reverse warning devices, and fire extinguishers should be




provided on all equipment used to spread and compact solid




wastes or cover material at the facility.



      (4)  Provisions should be made to extinguish any fires



in wastes being delivered to the site or which occur at the




working face or within equipment or personnel facilities.



      (5)  Communications equipment should be available on



site for emergency situations.



      (6)  Scavenging should be prohibited at all times to



avoid injury and to prevent interference with site opera-



tions, although controlled salvaging operations may be



permissable.




      (7)  Access to the site should be controlled and should



be only by established roadways.  The site should be accessible



only when operating personnel are on duty.   Large containers




may be placed at the site entrance so that individuals can




conveniently deposit waste.   The containers and the areas



around them should be maintained in a sanitary and litter-



free condition.





                            37

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                                                        154






      (8)  Traffic signs or markers should be provided to




promote an orderly traffic pattern to and from the discharge




area, and maintain efficient operating conditions.



      (e)  Disease and nuisance vectors shoxild be controlled



at the landfill disposal facility through minimization of



food and harborage and through initiation of additional




control programs if vector populations become established.




      (f)  Quantitative and qualitative records of solid



wastes received and location of disposal should be main-



tained and submitted to responsible authorities in accordance




with specific reporting instructions.



      (g)  A source of water should be provided at the land-



fill disposal facility for fire and dust control and for




employee convenience.



      (h)  A landfill disposal facility should be maintained




in an aesthetic manner.



      (i)  Following closure of a completed landfill disposal



facility a long term maintenance program should be initiated



and continued for as long as deemed necessary by the appro-



priate regulatory authority.
                            38

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                                                              155
S :"OM. j t_o_ri ric;

§ 241.'M6-1 General.  Monitoring can be  an  essential,  activity

in establishing, operating, and retiring a  solid  waste

landfill disposal facility.  Where possible,  monitoring

should be coordinated with State e\nd areawide water quality

management monitoring and assessment activities.

§ 241.206-2 Recommended Practices.  Solid waste  landfill

disposal facilities should be monitored  as  follows  for the

purposes of determining when contingency remedial action

plans should be implemented.

     (a)  Groundwater and Leachate Monitoring.

     (1)  A groundwater monitoring system should  be installed

for the purpose of detecting the impact  of  all landfill

disposal facilities which have the potential  for  discharge

to an underground drinking water source.

     (i) Publication EPA/530/Sw-Sli entitled  "Procedures

for Groundwater Monitoring at Solid waste Disposal Facilities"

should be consulted for additional information on this subject.

     (2)  In no case should groundwater  or  leachate monitoring

wells be installed through the bottom  o~ the  landfill proper

since such installation could result in  creation  of.a conduit

for the direct passage of landfill leachate into  underlying

ground- - .• ter.

     (3)  Samples from the monitoring  wells should be

collected and analyzed prior to disposal of solid waste

i-l a new landfill facility in order to obtain b^selina data..

     (4) Samples should be collected  fro:o all mo n i to r i n;.]

c\v'...--cj anil analy::;rl a: leas'.- on::c a y0.:ir.  Ttn analytical

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                                                          156




r-i.'tbocls specified in 40 CI-'R Pact 136, "GuLcle.lir.3S  Fs tablishing




'.i'ojt Procedures for the Analysis of Pollutants"  should  ba



followed.




     (b)  Facility Structure '"onitoring.




     (1)  All enclosed structures ab a solid waste .landfill




disposal facility should be monitored to detect  accumulations




of explosive or otherwise harmful gases which might pose a




safety hazard to facility employees and users.




     (2)  Explosive gases, typically methane, should  be




monitored for presence in the explosive limits with an



explosimeter.




     (3)  Toxic or asphyxiating gases should be  monitored on




a regular basis with appropriate instruments.




     (c)  Perimeter Soil Monitoring.




     (1)  Suitable probes should be installed in the  soil at




•tlie property boundary  surrounding the landfill  to enable




detection of gases migrating fro:;i the landfill.



     (2)  Explosive gases should be monitored for presence



above  the lower explosive limit.



     (3)  Toxic or asphyxiating gases should be monitored




on a regular basis with  appropriate instruments.
                              40

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                                                                     157
                  Guidelines for the Landfill Disposal

                            Of Solid Waste

                  Discussion Leader:  Mr. Truett V. DeGeare, Jr.


Question:  We would very much appreciate receiving at the Conference

           references related to:

           (l)  Guidelines for Determining Flood Flow Frequency

           (?)  Use of the Water Balance Method for Predicting
           (3)  Criteria for Classification of Solid Waste Disposal
                Facilities
           (4)  Procedures for Ground Monitoring at Solid Waste
                Disposal Facilities
           (5)  Guidelines Establishing Test Procedures for the
                Analysis of Pollutants

Answer:    I have those documents here.

           (1)  The first document is on flood flow frequency analysis and

           it is from the U.S. Water Resources Council.

           (2)  The second document is one of our publications which talks

           about estimating leachate production at solid waste disposal

           sites.

           (3)  The third document, which we call "the critera", is a

           proposed regulation which relates to land disposal of solid

           waste.  It is currently being finalized as a regulation, but all

           that I can provide at this time is the proposed criteria.  We

           have received substantial public comment on this proposed regu-

           lation and we expect to finalize it in July of this year.

           (5)  And the last document provides a listing and citations fcr

           recommended procedures for analysis of pollutants.


Question:  Let us know the reason why the word of "guidelines" and "guidance"

           has been separately used.

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                                                                            158
Answer:    The term "guidelines" is used in our law, and that is the term




           we had to provide as the title for this document.  The two terms



           "guidance" and "guidelines" are considered to be the same and



           are used interchangeably.  With regard to the use of "guidance",



           on Page 1, for example, we talk about guidance which is avail-




           able in other publications.  This approach indicates that al-



           though we discuss recommended practices in the guidelines, we



           do have other documents available that provide good technical



           gu idance.



Question:  Let us make clear the content of the definitions and how to



           conduct nuclear product.




Answer:    I think the definition of concern is that of "solid waste" which



           excludes certain categories of materials from being "solid waste."



           One excluded category is particular nuclear materials which are



           regulated by another federal agency and with other federal



           regulations.  This definition comes from our law and in effect



           tells us not to duplicate the work being done by another federal



           agency.  Therefore, we have not been dealing with the control



           of these nuclear wastes.



Comment:   The reason I raise  this  question is that in his paper Mr.  John



           Thompson's definition of solid waste appears to be somewhat in-



           congruous  with the definition in this paper.




Response by Mr. DeGeare:  I would never want to be responsible for reflecting



           improperly on my colleague's work.  John, will you yield to my



           definition?




Response by Mr. Thompson:  Yes.  Mine is incomplete.

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                                                                               159
Comment by Mr. DeGeare  • That happens once in a while.  Thank you for




           pointing that out.




Question:  Let us discuss how to compromise between minimisation of lea-




           chat e generation, and escape of decomposition gases.




Answer     Our concern here was that the sealing of ;he Jandfill




           surface could  in effect  force the migration of gases later




           ally within the soil.  In this section we want to make design




           engineers aware of the fact that by helping landfill practice




           in one respect they could be doing great harm in another




           and that both possibilities should be considered.




Question:  By reviewing the overall guidelines I got the impression that




           sometimes you put in some figures but sometimes you made your




           point without any figures.   I just wondered if the guidelines




           are designed for novices, e.g.   people who are not familiar




           with the problems.  What direction are you going to take  are




           you going to specify the guidelines with figures or are you




           going to leave them open?




Answer:    That's a good question.  In parts of the guidelines we have been




           very specific in providing what we consider to be good design




           numbers and the specifics are based on scientific research.




           In other cases  the guidelines include what has come to be




           sound and accepted engineering practice   In still other areas




           of the guidelines '.ve generally have been vague.   The document




           is not intended to be a cookbook design manual for novice




           engineers.   Rather,  it is intended to point out special




           concerns that we think are important with regard to landfill

-------
                                                                     160
           design and operation.   This has caused us tc  have  to make




           various judgements on  what is appropriate to  include as




           specific data and what is more appropriately  discussed




           in general terms.




Question:  Let us know the reason why the bottom of a landfill  should be




           1.5 meters or more above the seasonal high groundwater table,




           particularly from an historical standpoint in which it is pre-




           sumed there were other figures in the past.




Answer:    This is an area where we did not feel we could be  specific




           because of the extreme variability in soils and hydrogeology




           of sites across the country.  Our primary concern  is to point




           out that there should be separation—a soil separation




           most desirably—between the bottom of the landfill and the




           groundwater table.  The 1.5 meter specification is a suggestion




           and was obtained through discussions with various  State agencies




           that review engineering plans and they use this figure  as a




           general guide.  It is a good point that in many cases the




           presumption will not be true.  There will not be historical



           figures fcr the groundwater table.




Question:  So, in other words, those figures in the parentheses are not




           under regulations?




Answer:    Correct.The entire document is recommended; it is not required.




           The numbers in  parentheses are just suggested—nothing more.




Question:  Here is a very  interesting description (241.302 Leachate




           Control at Pages 24 and 25).So let us discuss further several




           points, such as leachate quality by age of fill, high molecu-




           lar weight, organic compounds, etc.  Let us discuss why

-------
                                                                     161
           the leachate will interrupt the biological process when about




           5/o of the total waste water is mixed.




Answer:    If I may, I will address the last part of the question first.




           The 5% represents the results of two studies that have been




           conducted.  These studies were conducted to try to determine




           what the break point was—the 5%— but did not get into the




           reason why the limit was 5%.  Therefore, I do not know why the




           break point value is 5%.  However, one could consider that it




           is due to the metals that are often found in the leachate.




           Or it could be just as well attributed to organics in




           leachate which happen to be foreign to the biological system




           at the waste water treatment plant.








Question:  Going back to the previous question relating to numbers, I am




           right to say that EPA will change figures whenever it feels




           that it is necessary?




Answer:    When there is new information that supports a different




           figure, yes.



Comment:   If there is such a case, I would like to be informed.




Answer:    Surely.  I would now like to go back to the first part of your




           question.  Since you were kind enough to provide an advance list




           of your questions, I was able to go back and obtain a copy of




           the research article on which this is based.  I have it here for you.



Question:  Let us discuss further experiment data concerning the recircu-




           lation of leachate onto the landfill.




Answer:    We have been involved with two recirculation projects.  Both




           projects made the concept of recirculation look very promising.

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                                                                162
When we did go to the field project in California, we were



concerned with equalizing surface distribution in leachate.



So in that case, since it was a research project, we used a



pretty fancy piping system to obtain equal distribution



throughout the surface.  This naturally would add to the



cost of the recirculation system.  However, I don't think



it would be necessary to go to that extreme in all cases.



Recirculation can be done feasibly without such sophisticated



equipment.

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                                                  163
ENVIRONMENTAL ASSESSMENT FROM THE VIEWPOINT OF
            SOLID WASTE MANAGEMENT
        THE FOURTH US-JAPAN CONFERENCE
           ON SOLID WASTE MANAGEMENT
                PREPARED BY

               MASARU TANAKA
   CHIEF OF SOLID WASTE MANAGEMENT SECTION
     DEPARTMENT OF SANITARY ENGINEERING
       THE INSTITUTE OF PUBLIC HEALTH

                 TOKYO,  JAPAN
                 MARCH,  1979

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                                                                      164
                             CONTENTS

                                                             Page

1.  Development Projects and Environmental Assessment  ....     1

2.  Environmental Impact of Solid Waste  	     8

 2-1  Solid Waste Versus Environmental Quality  	     8

 2-2  Mechanism of Solid Waste Impact  	     9

3.  Waste Treatment and Disposal-Related Impacts on the  ..    10
    Environment

 3-1  General  	,	    10

 3-2  From Generation to Discharge	    10

 3-3  Collection and Transport	    13

 3-4  Interim Treatment (Combustion, etc.)	    13

 3-5  Final Disposal (Inland landfill and shoreline  	    16
      reclamation landfill)

 3-6  Resource Recovery	    17

4.  Environmental Assessment Relating to Solid Waste  	    20
    Disposal

 4-1  Assessment of Impact  	    20

 4-2  Environmental Impact Assessment Procedure  	,    21


ACKNOWLEDGEMENT  	    31

-------
                                                                    165
           Environmental Assessment from the Viewpoint of




                       Solid Waste Management







                             Prepared by






                            Masaru Tanaka




                Chief of Solid Waste Management Section




                  Department of Sanitary Engineering




                    The Institute of Public Health




                             Tokyo, JAPAN






           Presented at the Fourth U.S.-Japan Conference on




           Solid Waste Management, Washington, D.C. U.S.A.




                           March 12VL3, 1979









1.   Development Projects and Environmental Assessment





     Projects subject to environmental assessment are those which produce




solid wastes which will cause serious adverse community effects if not




properly controlled, and those which discharge solid wastes which,




because of their quantity and quality, require prior coordination with




existing solid waste management systems.





     Such projects may be classified in many ways, but here it has been




done by type of waste:





(1)  Projects discharging mainly industrial wastes - plants, disposal




     facilities,





(2)  Projects discharging mainly general wastes - Buildings such as
                                  - 1 -

-------
                                                                 166
     condominiums, apartment-houses, offices, and





 (3)  Projects discharging materials related to construction activities




     such as sand, earth and debris.





     Since the extent of an individual project will affect its potential




 environmental impact, further classification on individual, area and




 regional scales is also useful.  Each of these classifications have an




 associated decision-making group.  For instance, area scale projects




 may be controlled by local government bodies, while regional projects




 may have prefectural or national oversight.  Table 1 gives s'ome examples




 of such a classification system.





     In general as the scale of a project increases, the responsibility




 for environmental assessment becomes more diffuse and the data available




 for assessment becomes less specific.  For individual projects, where




 design has been completed and waste quantities and types specified, the




 project planner should take primary responsibility for environmental




 assessment.  Housing projects and industrial parks are projects on an




 area scale.  If all the individual factories in an industrial park have




been specified, then environmental assessment can be carried out in the




 same way as for individual projects.  However, if factory specification




 is incomplete, the data base for assessment will be much less precise.




As an example, it may be difficult to forecast solid waste types and




 quantities, and subsequent environmental impact.





     On the regional scale, the number of groups involved in the




decision-making process is much increased.  This produces a problem for




 those responsible for environmental impact assessment.  Unfortunately




 these projects also produce greater quantities of wastes over large
                                 - 2  -

-------
                                                                                                                       167
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-------
                                                              168
geographical areas.  Because such projects and their environmental




discharges are often not well defined, preliminary assessment may well




be different from the individual project approach.





     Table 2 shows types of waste and types of discharging projects.




Waste sand and earth are discharged by all projects primarily during




the construction stage.  Industrial wastes, general waste from offices




and houses, and sludges are discharged through ordinary land use and




business activities.  It is necessary to recognize that all development




projects can be divided into two development stages — the construction




stage and the post-completion stage.  In addition, the discharging




mechanism and disposal methods depend on the type of wastes in the




vertical columns.  Recognition of these points should aid in determining




the wastes relevant to a specific project.  Table 2 is a general outline




for waste assessment.  However, each project must be individually




evaluated.  With reference to Table 1, waste disposal projects such as




incineration facilities and land reclamation projects can be regarded




as individual development projects.  Waste disposal facilities and




projects are listed as being subject to environmental assessment in the




ordinances of local governments on environmental impact assessment.




(See Table 3.)  Here the classification of solid wastes according to the




National Ordinance, "Wastes Disposal Act" is shown in Fig.. 1.

-------









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                                                                  170
      Table 3  Waste-related Projects Subject to Assessment

               under Environmental Assessment Ordinances
    Project
    Tokyo Metropolis
   City of Kawasaki
Refuse disposal
facility
(For new facility or expan-
sion)
                     3
Exhaust gas - 40,000m /hour
              or more

or, Drainage - 500m3/day
               or more
Incineration facility
with a land lot more
than 9,000m2, or with
a total building space
more than 3,000m^
Nightsoil
treatment
facility
(For new facility)

Drainage - more than
           500m3/day

Quasi designation"!"
Final Disposal
plant
(For new facility or expan-
sion)
Reclaimed land lot -
more than 10,000m2, or

Reclaimed volume -
more than 50,000m3
More than 1 hectare
(more than 15 hectares
in case of landfill
for sea area)
Industrial
waste disposal
facility
(For new facility or expan-
sion)

Exhaust gas - more than
              40,000m3/hour

or, Drainage - more than
               500m3/day
Incineration facility
with a land lot more
than 9,000m2, or with
a total building space
more than 3,000m2
f :   "Quasi-designation" means projects for which the Governor makes

     the decision whether the project is to be subject to environmental

     assessment, taking into consideration claims raised by the

     inhabitants and concerned parties of the area concerned.


* :   Draft Ordinance
                               - 6 -

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                                                  171




























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2 Sludge
3 Waste Oil
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                                                            172
2.   Environmental Impact of Solid Waste




2-1  Solid Waste Versus Environmental Quality




     Solid waste is often discussed together with air, water,  etc.



However, it should be distinguished from these categories.   Solid waste



is an offensive factor to environmental quality, just as exhaust gas is



to air quality and waste water is to water quality.  Exhaust gas and



waste water directly affect the air and water environments  and



consequently produce impacts and change environmental quality.



However, solid waste effects are not direct but result from waste



treatment procedures such as collection, transport, storage and disposal.



Exhaust control may be an effective means of maintaining air and water



quality at a specified level.  In other words, a fairly longtera



guarantee of control can be assured by construction and proper maintenance
                             ')


of treatment facilities which reduce pollution discharges.   On the other
                             i


hand, it is difficult to relate the discharge of solid waste to



environmental quality.  The relationship between solid waste and



environmental quality can be described as follows:




1)  The quantitative effect of solid waste discharge depends on the type



    of material and the method of treatment.  Solid waste has a potential



    impact on all phases of the environment.  For example,  sludge of a



    given quality and quantity will produce differring effects if stored



    in a airtight container, or combusted, or disposed by land fill.



    Consequently, discharge of the sludge itself can not be judged to



    cause a specific impact on environmental quality.




2)  When the solid waste disposal process from discharge to final disposal



    has been fixed, it becomes possible to forecast kinds and degrees of
                                 - 8 -

-------
                                                                  173
    environmental impacts at respective stages in the process.  It is




    in  then possible  to clarify quantitative/qualitative relationships




    between solid waste and environmental quality.  However, such




    relationships will vary depending upon the process stages and




    combinations.





3)  Sunce there are many means of solid waste control, it is not




    desirable to specify only one method to maintain given levels of




    environmental quality.  It is better to use a flexible approach by




    evaluating different alternatives.





 2-2 Mechanism of Solid Waste Impact





     Existence of solid waste itself is harmful to the environment.




It may  cause offensive odor, and produce adverse effects to public




health  and esthetics, and thus it affects both natural and living




environments.  These effects are considered as primary environmental




impacts.  However, the processes of stockpiling, storage, collection,




transport, treatment, disposal, and final return to the natural environ-




ment also may produce secondary environmental impacts.  The impacts




caused by the treatment and disposal process will usually result in




increases in some of the seven typical environmental pollutions (air,




water, soil, odor, vibration, noise, ground subsidence).  For example,




air pollution and water contamination may result from incineration,




and offensive odor, noise and water contamination may be caused by




landfill disposal.  Thus, solid waste management from discharge through




quantity reduction and decontamination has 2 aspects: — (1) It is a




direct cause of pollution and disruption of the natural environment,




and (2)  It may be harmful to environmental quality in itself.  These
                                 - 9 -

-------
                                                                   174
two aspects often correlate with each other.  The degree of impact




varies widely depending upon the treatment/disposal process applied.





     Fig. 2 shows the process of waste discharge through its natural reduc-




tion and the relationship between solid waste and environmental impact.









3.   Waste Treatment and Disposal-Related Impacts on the Environment





3-1  General





     There are three stages in the process of waste disposal:




(1) collection and transport, (2) interim treatment, and (3) final




disposal.  There is also a pre-discharge stage at the waste discharger's




site prior to collection of discharged waste.  In connection with (2)




and (3), there are also resource recovery processes.





     Table 4 summarizes the environmental impacts of solid waste with




respect to the major disposal methods for industrial, general and other




wastes.  The environments affected by solid waste include, in addition




to the representative seven pollutions, public health, the natural




environment (animals and plants, ecosystem, terrain) and esthetics.




Table 4 may serve as a general check-list of environmental impacts but




detailed studies are required for specific projects.





3-2  From Generation to Discharge





     Unless it is disposed of on-site, refuse generated in homes and




offices is temporarily retained and then collected and transported




elsewhere.  Generation of refuse is itself a source of offensive odor,




public health (flies, mosquitoes, rats in the residence), esthetic




degradation and occupies space.  If refuse generation is considered as
                                - 10 -

-------
                                                              175
                   Occurrence/existence of waste
                      Environmental Pollution
                                   Primary environ-
                                   mental impacts -
                                   offensive odor,
                                   damage to scenery,
                                   increased fly,
                                   mosquito, rat, and
                                   other vectors
             Primary Environmental Protection Measures
Stockpiling,
maintenance
 Collection,
 transport
Treatment
Disposal
                     Environmental Pollution
                (Secondary Environmental Impacts)
Offensive odor,
damage to scenery,
waste water,
public sanitation,
privately owned
space
 Noise,  offen-
 sive odor,
 traffic,
(labor accidents)
Waste water,
harmful gas,
residue,
soot/dust,
noise, offen-
sive odor,
vibration
Waste water,
harmful gas,
hazardous substance,
offensive odor,
(accident),
damage to scenery,
land utilization
                                                      • Secondary
                                                       Environmental
                                                       Protection
                                                       Measures
                         Natural Reduction
           Fig.  2  Flow of Waste and Environmental Impacts
                               - 11 -

-------
                                                                   176
Table 4  Major Methods of Waste Disposal and their Environmental Impacts
\Environmental
impacts
Disposal \v
method \.
Pre-exhaustion stage:
Stockpile
Selection
Collect ion/ transport
process:
Collection by truck
Transport by truck
Relay operation
Interim treatment
process:
Smashing/pressing
Dehydration/drying
Incineration
Post-treatment
Final disposal process:
Landfill for recla-
mation
Landfill for sea area
Conversion into
resources:
Recovery of substance
Recovery of energy
H-
n
A

A
A
f|
O
o
©
©
A
A
O
£
rt
(0
n
A


©
0
O
O
o
H-
A


0
©
0
©
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A

O
0
O
O
O
O
A
O
0
o
A
Vibration/
noise


©
O
©
A
A

A
A
Land subsidence



0
A
A

Total hazard*


O
©
O

O
o

Public sanitation
0
A
A
O
O
A
A
O
O
A
A
A
Natural
environment
O


O
o
0
A
A
*  Traffic/road hazards due to concentration of waste carrying cars.

               A •  Environmental impact observed.
               O '•  Consideration to environment required.
               © :  Protection measures for environment required.
                                - 12 -

-------
                                                                177
the primary factor, the storage of refuse can be considered as a




secondary factor, which develops offensive odor, water contamination




by waste water, and disruption in the areas of public health, esthetics




and occupancy of private space.  The impacts by types of refuse




containers are indicated in Table 5.





3-3  Collection and Transport





     Collection and transport of refuse are also considered as secondary




impact factors from the above standpoint.  The degree of disruption




they will give to environmental quality vary depending upon types and




quantity of refuse, forms, means, place and frequency of collection.




During these processes offensive odors and contamination of and around




collection spots by the uncollected refuse, traffic congestion and




noise during refuse collection and air pollution by exhaust gas may




occur,





     Table 5 shows examples of pollution by forms of collection and




transport.  The word 'collection' is used here to mean the process of




loading the refuse into a garbage carrier from storage sites, and




'transport'  to mean the process of carrying the loaded refuse to an




interim treatment plant- or to a final disposal plant.  Typical means




of transport are roads, railroads, pipelines and barges.  During




transport, environmental pollution may be produced by splashing or




blowing of soiled water and refuse,  and automotive emissions and noise




due to traffic congestion caused by concentration of garbage carriers.





3-4  Interim Treatment (Combustion,  etc.)





     Interim treatment for refuse aims at accelerating the oxidation




of refuse.  Solid waste undergoes physical, chemical and/or biological
                                 - 13 -

-------
                                                                178
Table 5  Collection/Transport-related Impacts upon the Environment
\Environmental
impact
Environmental ^v
pollutant factor ^v
Generation/ Stockpiling:
Garbage box of conven-
tional type -
(polyethylene bucket,
underground garbage
box)
One-way container- -
(paper bag, poly-
ethylene bag)
Others -
Container
Dust-chute
Disposer
Collection/Transport :
Forms of collection -
Laissez-faire
Door-to-door
Station
On request
Collection time -
Daytime
Nighttime
Collection frequency -
Regular
Irregular
Transportation -
Automobile
Rail/ Subway
Pipeline
(slurry transport)
Offensive odor
O
O
0
O

O
o
0
0


o
o



•z
o
H-
CO
n



o

0
o
0
o
0
o


o
o

Air pollution





0
o
o
o




o


Vibration
















Water contamination




O











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-------
                                                                   179
treatments up to the stage where natural purification mechanisms will




be maintained.  The basic purposes of interim treatment are (1) to




reduce refuse volume, (2) to biologically stabilize for sanitary




handling, and (3) to nullify hazardous substances.





     In general, quantities and forms of industrial waste vary




depending on the type of industry.  Those of general waste fluctuate




regionally and seasonally.  It is necessary to choose a suitable




interim treatment method so that the interim process itself does not




become a source of secondary pollution.





     The combustion method is sanitary as both refuse and germs and




insects can be destroyed.  It also improves oxidization and reduction




of refuse volume, and facilitates its disposal by stabilization.




In addition, it offers the possible utilization of the refuse as fuel.




This method is one of the most effective means of disposal.  However,




air pollutant emission and water pollution by contaminated cooling-




water and ash-quenching water are of particular concern and counter-




measures for these are essential.  Preventive measures must also be




taken against offensive odor and noise.





     Through pre-disposal treatments such as smashing, pressing and




dehydration of solid waste (especially for construction waste material




and mining waste) serious impacts may be produced due to dust, noise




and vibration.  Offensive odors generated during drying of organic




sludge also is an adverse environmental impact.  Contamination of air




and soil by dehydration of waste acid, waste alkali and sludge and by




supernatant water present serious problems, and especially so if they




contain heavy metals and other harmful substances.  Esthetic and
                                - 15 -

-------
                                                                      180
public health aspects also cannot be disregarded.





     The post-treatment given to dispose of exhaust gas and water,




and dust and residue generated during interim treatment raises the




possibility of contaminating water with soot collected during wet




scrubbing, contaminating air by the dry treatment,  and contaminating




water and soil by treatment for residue.





     As for combustion treatment, a very large volume of water is




consumed for drainage of cooling water, water jets, refuse pits,  or




ash pits, in addition to the drainage of soot and dust cleaning water.




When underground water is used for this, ground subsidence may become




a problem.




     Aside from combustion, thermal treatment by way of thermal dis-




composition in a fluidized incinerator, of gasification, of melting/




solidification in a melting furnace, and so forth will produce impacts




in the atmosphere as well as those caused by other interim treatment




methods.





3-5  Final Disposal (inland landfill and shoreline reclamation landfill)





     There are two final disposal methods of refuse; landfill and ocean




dumping.  Table 5 deals with the landfill method as a major means of




final disposal.  Both inland and shoreline sites are effective sanitary




landfills, but still require consideration and effective control of




the following impacts to the environment:





(1)  Inland landfills may contaminate soil and underground water and




     other streams by leachate;




(2)  Shoreline landfills require the same considerations as for inland




     sites but with an additional concern for the ocean waters in the
                                - 16 -

-------
                                                                     181
     immediate vicinity of the landfill.  The characteristics of the




     environmental impacts caused by landfill disposal are summarized




     in Table 6.





 3-6  Resource Recovery





     Resource recovery processes may be a valuable method of solid




waste disposal.  However, not many of them have been established as




usual disposal method for both industrial and general wastes.  Disposal




processes of this type are simply classified into the following:




 (1) Substance Recovery - This includes two kinds of recovery such as




 (a) to separate and recover serviceable substances out of the waste,




and (b) to convert the waste into serviceable substances by chemical




and/or bacterial treatments.  Conversion of urban refuse and organic




sludge into compost is one example; and (2) Energy Recovery - This




includes such processes as conversion of organic waste into gasified




or liquefied fuel by thermal decomposition, and use of the. heat




generated during direct combustion of the waste by way of hot water,




steam and electricity.





     However, these disposal processes may also have adverse environ-




mental consequences.





     High-rate composting is usually done within one week of aerobic




digestion of refuse, and may be utilized as a fertilizer on farm land




after a few months of stabilization.  It is also sometimes used as a




soil conditioner.  In either case, addition to the soil may given some




impacts, the most serious of which is contamination of soil and under-




ground water by the harmful components of the original refuse.   The




offensive odors from the original organic refuse and during handling of




the semi-processed compost may also be of concern.
                                 - 17 -

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                                                              184
     Energy recovery by refuse incineration requires consideration of




air pollution and water contamination by waste water.





     It should be recognized that in contrast to ordinary production




processes, conversion of wastes into resources has as its primary




objective the adequate disposal of wastes.   Therefore, even greater




care should be exercised with respect to potential environmental




impacts than with other disposal methods.  It would be undesirable to




neglect the environmental considerations of such a process, just




because a relatively higher return is attainable in terms of resource




recovery.









4.   Environmental Assessment Relating to Solid Waste Disposal





4-1  Assessment of Impact





     The most important consideration in assessing the adequacy of




solid waste disposal for  general development projects is that suitable




control procedures be used for each step from generation to final




disposal.  Further assessment requires consideration of the following




points:





(1)  Treatment and disposal of waste should be done by a method which




     produce the least impact on the environment.




(2)  It is important that the selection of  a landfill site is in accord




     with an overall land utilization program and that a long-range




     and extensive administration system is established to guarantee




     environmental protection after completion of the landfill.
                                - 20 -

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                                                                      185
     The "Guidelines for Constructing Waste Disposal Facilities" issued




by the Ministry of Health and Welfare state that "in planning improvement




or construction of a waste disposal facility, prior assessment of the




countertneasures for exhaust water and gas, offensive odor, vibration,




noise, etc. discharged by the facility should be effected in order to




prevent environmental pollution".





4-2  Environmental Impact Assessment Procedure





     In the above paragraph, we have pointed out that estimates of




environmental impacts by waste must be made based on an independent




and many-faceted assessment since such impacts are fairly different




from those by waste water, gas, or noise.  In addition to this, it




must be also pointed out that because of the peculiarity of solid waste




it is also in itself a potential cause of pollution, which makes the




impact assessment process different from those for the other seven




typical pollutions.  The forms of impact upon environment vary widely




depending upon the methods of treatment and disposal.  Other pollutants




can be evaluated for environmental impact by considering generation




control at the source.  The procedure for impact assessment of solid




waste is a very complex one in that the assessment must be carried out




both on the control measures for the waste and on the control measures




for the secondary pollutants generated during waste treatment and




disposal as well as the methods of treatment and disposal themselves.





     The following is a summary of the impact assessment process for




solid waste (see  Fig. 3).  The data necessary for assessment are shown




in Table 7.
                               - 21 -

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                                                              186
ex
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                       Table  7  Information to be required for Assessment Work
    Work Stage
                                                          Information Required
Assumption of
activities to
generate wastes:
                    The plan and project data are the basic information, but also data on waste generation.
                    EX) Construction stage — Structure of building, construction method, raw material,  terrain,
                                              quality of earth, etc.

                        Operation stage 	 (In the case of industrial park)   Kinds  of  industry  to be  located,
                                              manufacturing process, disposal processes of waste water and waste
                                              gas,  raw material, etc.

                                              (In the case of housing projects)   Population,  family composition,
                                              income, area service facility plans,  etc.
                    Information on volume and quality of the waste against which the assumption of the occurrence-
                    related activity is made (original unit of waste volume, similar examples for the same type of
                    industry, etc.)

                    Information on effective utilization, conversion into resource
Forecasts of
volume and
quality of waste:
Assumption of
disposal-related
activities:
Flow of waste dis-
posal and quanti-
tative determina-
tion of pollutant
factors:
Establishment of
assessment
standards:
Forecast of
environmental
impacts:
                    Information on the forecasted volume/quality of waste (standard,  variance),  the regulations
                    under laws and ordinances and their criteria,  administrative guidance,  guidelines,  etc.

                    Actual status of waste and its disposal in adjacent  areas
                    Information on methods of disposal and prevention of secondary  pollution

                    Katural environment of the adjacent areas (atmosphere,  water, rainfall,  etc.)

                    Information on social environment (land utilization, situation  of road,  etc.)

                    Information on capability of the  related administrative body (implementation of assumed
                    activity,  maintenance and custody)
                    Information on the balance of  materials  in each disposal  process  and  on  the volume  of  pollutants
                    Information on the reduced volume  of  pollutants owing  to  pollution  control technology
                    Information on control under  laws  and  their  criteria,  administrative guidance,  guidelines

                    Development level of  technologies  of disposal  and  secondary  pollution  control

                    Information on natural/social environments in  the  adjacent areas

                    Information on the final  disposal  place
                    Outline  of  the  assessment  process  related  to possible environmental pollution

                    Information on  disposal  sites  (disposal  land owned by the  disposal contractor,  disposal
                    land  owned  privately)

                    Information on  natural/social  environments where  impacts are expected to occur
      Remarks:   In an actual assessment work,  all of the above information is  not  necessarily required,  and  other
                data may be needed aside from  the above.

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                                                                    188
1)   Estimate  of  Solid Waste  Generation





         As indicated in Table 3, various development projects produce




     various wastes.  It is desirable to control the generation of




     solid wastes, just like other environmental pollutants.




     All of the solid wastes which may be produced by a particular




     project should initially be check-listed.  Some development projects




     may produce wastes elsewhere outside their planned areas during




     the course of construction.  For example, in the case of a large




     factory,  the wastes generated by related sub-contracting factories




     and employees' families should be taken into consideration, and




     such wastes should be included.  The checklist should contain all




     the possible wastes classified by project and their work stage,




     and by type of waste.  Then, the volumes and solid waste qualities




     (including those from generation control measures) should be




     estimated.  Any waste, which is not quantitatively or qualitatively




     significant can then be excluded from further consideration on




     condition that the reason for such exclusion be stated.





         Estimates of wastes must be made in such a manner that the data




     obtained  is available in a form so that treatment and disposal




     processes can be chosen to minimize the occurrence of the secondary




     pollutants.  In other words, the information on the generation of




     wastes should be made available not only for estimation purposes




     but also  for selection of the methods for treatment and disposal




     of the estimated wastes, and for evaluation of environmental impact.




     In particular, hazardous waste evaluation should be carried




     separately from those for other wastes.
                                  - 24 -

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                                                                189
2)   Treatment and Disposal Activities  Assumptions




         At  this  stage,  the treatment  and disposal  system will be




     specified for the wastes estimated in section  (1).





         Fig.  4 shows the  flows of industrial waste treatment and




     disposal processes.  All the wastes generated are to be disposed




     of  through these flows.  General waste and other wastes will




     generally not go through such a complex process as for industrial




     wastes.   However, when general waste disposal is contracted for




     by  a city, town, or  village administration, the wastes will be




     processed according  to the contract flow shown  in this Fig. 4.




     The treatment and disposal activities assumptions mean the




     specification of the flow path in  Figure 4 through which the




     estimated waste is to  be disposed.  The following points should be




     noted for these assumptions:





     i)   The treatment and disposal process should  be specified as




         concretely as possible.




         This specification requires solid waste quantity and quality




         estimation for  collection, transport, interim treatment and




         final disposal, as well as for the overall process.  Collection




         and transport,  interim and final treatment and waste disposal




         sites should be specified at  this stage of evaluation.




         If  a treatment  and disposal plan is incorporated into project




         planning at this  stage, the disposal plan  should be adopted.




         However,  if no  disposal plan  has been determined, one should be




         developed in as concrete a form as possible.
                                  -  25  -

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                                                                                                  190
                                    [Manufacturing Process]—
                                         Primary  Waste
 (Self disposal)
                                                    Primary waste to
                                                    be disposed
                                                              Primary waste  to
                                                              be  stilized inside
Primary waste to
be stockpiled




                         (Stockpiled inside

                                I
                         (Contract)
Waste to be
subject to
final disposal
 -(Land-
 fill)

^_( Ocean
 dumping)
                                                         i
                                            Waste  to  be sold/transferred
       I              \
r-(Disposal)   (Re-utilization)
                                (Disposal)
(Re-utilization
inside)

(Sale)	
                                                        -(Stockpiling)
c
rt
M
4J
o en
r-l (3
18 -P
W Ul
 "(DisposalT
                       Waste disposed
                       by contract
                        -(Treatment)
                            _J	
         (Stockpiling)-
                                         (Re-utilization inside)

                                               f	
                                               (Sale/transfer)-
                                        N.B.  : The  inside flow is same as
                                               in the  stage of waste
                                               generating enterprise.
                                                                                        a o
                                                                                        W 13
                                                                                                         in  c
                                                                                                        •H  O
                                                                                                        Q  o
               Fig. 4  Flow of Industrial Waste  -  Its  Generation through Disposal

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                                                                   191
      ii)    The assumed activities  should be technically feasible




            and practical, because  they will largely determine the




            actual  effect of  the environmental impact assessment.




      iii)   Preventive measures against secondary environmental




            pollutant factors generated during the  treatment and




            disposal processes should be included as one of the




            assumptions.  In  the process of waste treatment and disposal,




            there will occur various pollutant considerations, in




            addition to the seven representative pollutions, and




            assumed activities should include preventive measures for




            these as well.  In planning preventive measures, reference




            should be made to the disposal standards and the standards




            for construction and maintenance of waste disposal facilities




            stipulated in the Waste Disposal and Public Cleansing Law.





3)    Quantitative Determination of Pollutant Factors to be Generated in




      Waste Flow and Treatment and Disposal Processes





      The environmental impact assessment of solid wastes should be




based on the three assessment indices described in section  4-1.




Consequently, it will become necessary to pick the polluting elements




which are expected to occur in the given waste flow and the treatment




and disposal processes and then to arrange the data for the purpose of




assessment.  The waste flow, and especially the quality and quantity of




the waste for final disposal are essential information for coordinating




the disposal with other plans and projects,  for securing long-ranged




and extensive environmental protection, and for maintaining the treat-




ment  and disposal system in the future.  Quantitative determination of
                                - 27 -

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polluting elements is also essential as the information necessary to




forecast the degree of impact upon the environment during the treatment




and disposal process.





4)   Forecast of Environmental Impacts





     In this step, a forecast is to be made in regard to the degree of




explicit impact of polluting elements and the flow of waste disposal




upon the neighboring environment.





     The data from item (3) is used to in order to estimate and assess




the impact of the seven typical pollutants on environmental quality.




Consequently, the forecast of polluting elements peculiar to solid




wastes and the possibility of maintaining the waste management system




are most important.





5)   Determination of Assessment Indices  (see Section 4-1)





6)   Primary Assessment





     The forecast degree of environmental impact (item 4 above) is to




be evaluated in light of the assessment indices (item 5 above).  The




impacts of assumed flow and polluting elements must be checked to




meet assessment standards, and the results of this procedure should be stated.





7)   Re-review of Assumed Activities





     When all standards are met in the primary assessment, this process




will not be required.  If not, the assumed activities are to be re-




reviewed retroactively in the processes of plan or project, treatment




and disposal, or of the preventive measures for secondary polluting




elements so that the assessment standards should be met.
                                - 28 -

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                                                                      193
8)   Final Assessment and Reporting





     After going through the above whole process, a report should be




compiled, confirming that the assumed activities can meet the finally




established assessment standards.  When there are many uncertain parts




in a plan or project, it should be explained in the report that the




environmental impacts of the uncertain parts do not alter the entire




project.  Means to follow-up the uncertainty should also be specified




in such impact assessment.





     The summary of the process for environmental impact assessment




of waste disposal is as given above.  The reporter of the assessment




results should state in his report the above-mentioned forecast of




occurrence, assumption of activities, assessment standards and assess-




ment results in this order so that a third-party may be able to




examine if the assessment results are adequate.  In this connection,




we would like to point out particularly that the reporter should




clarify the capability of the project promoter to undertake the




assumed activities and the criteria applied for assessment.




Such a statement will be essential for the study of his report by a




third-party.





     Inevitably in large projects, the waste generation and the




assumed activities for waste disposal cannot be completely definite.




A good example is a large industrial park whose occupants are not yet




decided.  In such a case the assumptions of polluting factors and




treatment activities have great importance, and have influence upon




the validity  of the given assessment.  Therefore,  the assessors must




obtain as much information as possible about the plan from the point
                              - 29 -

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                                                                 194
of the planner.   The activity assumption must also be specified as




precisely as possible and must be practical and feasible.   It will




further become necessary for the assessors to determine whether there




is the possibility that the assumed activities may be revised to




give adverse effects upon the environment, and they should suggest




necessary countermeasures when such a possibility is forecast.
                                 30 -

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                                                                 195
                         ACKNOWLEDGEMENT







     Here the writer wish to thank to Dr. S. Gotoh, Mr. M. Yagishita and




Mr. A. Shimazaki and others whose ideas and opinions are very significant




for the preparation of this paper.




     Appreciation is also expressed for the coorporation and assistance




of the Japan Environmental Sanitation Center to compile and translate




this report.






References:




  1.  M. Yagishita, "Environmetal Impact Assessment from the View of




      Waste", the 6th Environmental Problems Symposium, Japan Society




      of Civil Engineers, Aug., 1978.




  2.  M. Tanaka "Preparation of Environmental Impact Statement for




      Solid Waste Management", the 5th Environmental Problems Symposium,




      Japan Society of Civil Engineers, Aug., 1977.




  3.  Environmental Information Science Center, Research Group for




      Environmental Impact Assessment System, "Informations Concerning




      Environmental Impact Assessment", Environmental Information




      Science Center,  1976.
                                 - 31 -

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                                                                        196
  Environmental Assessment from the Viewpoint of Solid Waste Management
                Discussion Leader:  Dr.  Masaru Tanaha
 Question:  Are the projects listed in Table 2 subject to environmental

            assessment under national law even where they are privately

            financed?

Answer:     We don't have a national environmental assessment law.   We have

            one currently under discussion and some people are in hopes

            that we will have one.   Regarding the financing issue,  in my

            opinion, we shouldn't separate those projects that are pri-

            vately financed from those that are publicly financed.   Any

            project which may have a public environmental impact should

            be subject to an environmental assessment.

 Question:  Regarding the management of assessment programs, does it involve

            public hearings?  Is it implemented through facility permits

            or land-use (zoning) permits or both?

 Answer:    Yes, public hearings are included in assessments.  We have

            two established assessment ordinances in Kawasaki City.

            Many other cities are preparing their assessment ordinances.

            Both facility permits and land-use permits arc used.

 Question:  Who is responsible for long-term impacts, ecpeci^lly in the

            case of completed landfills?

 Answer:    In Japan e'ven after the completion of a landfill the owner or

            operator is responsible for longterm  impacts.  ri'h,ey are res-

            ponsible for treating leachate for a number- of years until

            there  is no longer a problem.

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                                                                 197
Question:  Do you require financial bonding?




Answer:    W.e do not require   it.  There is no snrh thing in Jaoan.




Question:  Who  is responsible  for costs of mcnitoring?




Answer:    Same as with  the landfill—the owner or operator.




Question:  Table 6—"Structure of Landfill Site" — please describe




           differences between Isolation Type, Control Type, and




           Stable Type.




Answer*:    Table 6 describes three different types of landfill.  Isolation




           type is for hazardous waste.  The landfill itself is completely




           isolated from other environments, so no leachate ever goes out




           of this landfill.  It is sealed by concrete structures to con-




           tain the leachate.  Control type of landfill is for domestic




           solid waste.  The third one is a stable type landfill.  This




           stable type landfill  is for inorganic waste, like construction




           material; this does not create any water pollution problem




           since it has  no organic material.




Question:  Is on-site "self-disposal" assessed and regulated?  For example,




           disposal of industrial waste on the industry's property?



Answer:    The answer is, it should be.  We don't have a national assessment




           law.  But based on our Solid Waste Disposal Act, Articles,




           even private  property for solid waste disposal should be re-




           ported to the authorities and the local government has the right




           to inspect at  any time.  So any solid waste disposal sites




           should be assessed and even now it is regulated.



Comment:   I'd like to make a couple of observations.   I like the compre-




           hensive perspective that you properly take.   In my opinion,

-------
                                                  198
when we speak about impacts related to solid waste activities,



we should take a broad perspective of the environmental



impact rather than narrowly  looking at air pollution or



water pollution, as some engineers do.  When you introduced



your paper, you spoke of two assessments: one, of the



assessment of solid waste generation and one of the assess-



ment of solid waste management systems.  The focus that



we have seen in this country has been on the second—the



assessment of solid waste management systems.  For example,



disposal facilities.  We spoke in 1976 about the difficulty



of siting—obtaining disposal sites—and the United States



is no better off today than we were then.  There is great



public interest in assessments related to disposal facilities.



Regretfully, there is not the concern for assessments of



solid waste generated by other types of new projects such



as new towns.  The focus is on the disposal facility, rather



than on the facility that is generating the waste.

-------
                                                                        199
                 LEACHATE TREATMENT DEMONSTRATION
                        Bernard J. Stoll
              U.S. Environmental Protection Agency
                        401 M Street S.W.
                   Washington, B.C. 20460
                            ABSTRACT



     This paper reports the results of three years of operation of a

solid waste landfill leachate treatment plant.  This plant incorporates

chemical, physical, and biological unit processes and was constructed to

enable operation in several sequences of unit processes.  The processes

include:  equalization, lime precipitation, sedimentation, ammonia

stripping, activated sludge, carbon adsorption, and chlorination.



     The purpose of this project was to demonstrate the treatment of land-

fill leachate at full scale in four treatment sequences.  The plant is

supplied by an adjacent, lined landfill which generates about 20,000

gallons per day of leachate high in organic matter, ammonia, and heavy

metals.

     Of the treatment sequences demonstrated, that sequence which incor-

porates equalization, lime precipitation/clarification, ammonia stripping,

activated sludge treatment and chlorination (in that order) has been

the most effective in achieving the discharge standards for this waste-

waster treatment facility.  This treatment sequence has been found

capable of meeting the discharge standards except BOD and lead, which

have been occasionally exceeded, and ammonia, which has seldom been

achieved.

-------
                                                                         200
                             BACKGROUND




EPA has been studying the treatment of landfill leachate, because of the




potential for adverse effect on ground and surface waters for several




years.  Most investigations were laboratory-scale or occasionally pilot-




scale treatment systems.  In early 1975 the Office of Solid Waste became




aware of initiation of construction of a leachate treatment system to




serve a lined landfill in Pennsylvania.  That State had awarded  an




operating permit for a mixed municipal solid waste landfill which was




to be constructed above grade, underlain with and surrounded by a




dike covered with a sprayed asphaltic compound, in 1970,  The permit




included a provision requiring leachate treatment and discharge to the




Delaware River at such time as the dike became filled with leachate to




within two feet of overflowing.  The Delaware River Basin Commission




subsequently (1974) awarded a permit for discharge of treated leachate




from the landfill to the Delaware River during the high stream flow




months of December through April in accordance with the effluent quality




criteria listed in Table 1.




     Applied Technology Associates was awarded a demonstration grant in




late 1975 to evaluate the efficiency and economics of full-scale treat-




ment of landfill leachate at the GROWS (Geological Reclamation Operations




and Waste Systems, Inc.) landfill, located in Bucks County near Tullytown,




Pennsylvania.  The evaluation was to comprise two years of full-scale




operation of this leachate treatment system which incorporated chemical




physical and biological treatment.

-------
                                                                      201
                         THE SYSTEM







     The leachate treatment system designed to meet the needs of the




GROWS landfill was a modification of a package type sewage treatment




plant.  The system consisted of a flash mixing chamber for lime




addition to influent leachate prior to introduction to a cylindrical




clarification unit.  Clarified effluent was then to be introduced




to a prefabricated aeration/sedimentation unit for activated sludge




biological treatment, prior to discharge.




     In order to determine design parameters for the leachate treat-




ment system, samples of the landfill leachate were obtained and used




for operation of a laboratory bench-scale treatment system.  The




leachate characteristics upon which plant design was based are presented




in Table 2.  Limited sampling in the early stages of landfill operation




yielded these characteristics which will be shown later as having changed




dramatically.  The ultimate design flow for this system









     During the three years of this demonstration the original design




has been modified significantly through addition of two lagoons.  The




first lagoon was constructed to serve as an ammonia stripping pond




following lime addition to the influent leachate.  The second lagoon,




added late in the project, serves as an equalization pond constructed




ahead of the entire leachate treatment system.




     The current facility is shown schematically for System 1 in Figure




1.  Detention times in the various units are about 2 days in each of the




lagoons, 2 hours in the reactor clarifier, and 6 hours in the aeration

-------
                                                                                202
              chambers at the design flow of 100 gpm.  Since current flow rates  are

              only about 15 gpm these detention times should be increased accordingly.

                   As a result of award of the demonstration grant the  facility  has

              been equipped with a laboratory trailer to enable prompt  analysis  of

              samples to enable system evaluation and operation.
                  TABLp  1
       SUMMARY OF EFFLUENT CRITERIA*

                     Maximum  Concentration
Parameter                  mg/liter
BOD5
Ammon ia-Ni trogen
Phosphate
Oil and grease
Iron
Zinc
Copper
Cadmium
Lead
Mercury
Chromium
100.0
 35.0
 20.0
 10.0-
  7.0
  0.6
  0.2
  0.02
  0.1
  0,01
  0.1
^Commonwealth of Pennsylvania Department
 of Environmental -Resources and  Delaware
 River Basin Commission.
            TABLE 2
DESIGN LEACHATE CHARACTERISTICS
                                              Constituents
                                      Raw Leachate*
               BOD5
               Sus.  Solids
               Total Solids
               Percent Volatile
               PH
               Chlorine
               Iron,  total
               Zinc
               Chloride
               Organic Nitrogen
               Nitrate
               Sulfate
               Copper
               Hardness
               Alkalinity
               Color, standard units
               Flow, mgd
               Temperature,  °F
                        1500
                        1500
                        3000
                          55
                         5.5
                         200
                         600
                          10
                         800
                         100
                          20
                         300
                           1
                         800
                        1100
                          50
                       0.144
                          80
                                              *A11 units are mg/1 except pH, color,
                                               flow, and temperature.

-------
                                                                                   203
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-------
                                                              204
                           DISCUSSION









     As previously indicated the design leachate characteristics pre-




sented in Table 2 have been shown to be highly inaccurate.  Over the life




of this project leachate volume and strength have fluctuated widely but




have tended to increase overall.  Table 3 presents the quality of the




raw landfill leachate for each year of this project and the




average leachate quality, over time.  To further depict the variability




of raw leachate quality Figure 2 is included.  As seen in Figure 2, the




COD has varied from as low as 5000 mg/1 to as high as 50,000 mg/1.




     Anyone who has worked with landfill leachate is familiar with




such fluctuations in leachate quality.  Elaboration on this topic is




considered appropriate in this report in that it demonstrates one of




the problems encountered by both the designer and operator of such a




leachate treatment facility.  Since, as in this case, it is often




necessary to design the leachate treatment system either at the design




stage of the landfill or in the very early stages of landfill operation,




the designers must rely upon the literature for "typical" leachate




quality modified by leachate quality prediction techniques.  In this




situation, young landfill leachate and prediction techniques were inade-




quate.




     From the operator's standpoint leachate quality variations can cause




serious difficulty in attempting to automate chemical addition to  the




influent raw leachate, such as lime.  Only frequent analysis of influent




leachate and subsequent adjustment of chemical feed can accomplish the




desired result.  Significant variation in the organic strength of influent

-------
205














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-------
                                                                  206
leachate to a biological treatment element is also a problem, but the


buffering capacity of activated sludge ameliorates this problem somewhat.


Construction of an equalization lagoon upstream of the treatment facility


was the "solution" selected to reduce the degree of quality fluctuation


at this facility.


     Construction of this leachate treatment facility was completed in


late 1975.  Start-up attempts were initially frustrated by freezing


temperatures until Spring of 1976.  Three attempts at establishing an


activated sludge culture by acclimation of waste activated sludge "seed"


from a nearby sewage treatment plant were unsuccessful. Bench-scale


simulation of the biological unit process indicated that the landfill


leachate was deficient in phosphorus and had an excessive ammonia concen-

                                )/
tration which was thought to be tyoxic to the biomass.  The phosphorus


deficiency was immediately corrected by addition of phosphoric acid ahead


of the aeration tanks.  In order to deal with the high concentration of


ammonia, the twin aeration tanks were modified from parallel to series


flow.  In the first tank the pH was raised to greater than 10 to enable


ammonia stripping by aeration.  After several weeks of operating in this


mode, it was concluded that there was insufficient surface area for


effective ammonia stripping.  This decision led to construction of the


first of the two "add-on" lagoons.


     Construction of this lagoon equipped with a diffused aeration system


proved effective in reducing influent ammonia concentrations by greater


than 50%.  A leachate acclimated biomass was finally achieved in July 1976.


This biomass was again lost to freezing weather during the 1977-78 winter


and reestablishment of the biomass in the Spring of 1978 was somewhat less


difficult.

-------
                                                                        207
       FIGURE 2.   RAW LEACHATE CHEMICAL  OXYGEN DEMAND
              (Note change  in scale on ordinate.)
   25
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       DEC.   JAN.  ?£3.  -AR.   *?<*.  M/iy   ji.NE   JULY  *UC. SEPT.   OCT.   «*OV
           l?77

-------
                                                                 208
     As indicated earlier,  chemical/physical followed by activated




sludge treatment was the original treatment design and the sequence




expected to be the most effective.   This sequence (referred to as




System l) was initiated on  August 1, 1976,  (following acclimation




of the activated sludge to  leachate) and evaluated through April 30,  1977.




     Operation in the System 1 sequence involves chemical addition,




primarily lime, to the raw  influent leachate to precipitate dissolved




metals and reduce suspended solids.  Following clarification the leachate,




now at a pH in excess of 10.5 is introduced into the aerated ammonia




stripping lagoon.  The lagoon effluent is neutralized with acid, if




necessary, and supplemented with phosphoric acid prior to introduction




into one of the two parallel activated sludge chambers.  Clarified




effluent from the biological system is either returned to the landfill




or discharged to the Delaware River depending upon effluent quality




and the time of year.  Effluent is chlorinated before discharge to




the Delaware River.




     This same System 1 sequence was retested in July and August 1978




with the following modifications:




     1.  raw leachate was first introduced into an aereated equalization




         lagoon,




     2.  the activated sludge aeration chambers were operated in series




         instead of in parallel, and




     3.  the flow rate was  only about half that of the previous operating




         period  (i.e. 10,000 vs 22,000 gpd).




     Concurrent evaluation of System 2 also took place during these




periods since the System 2 sequence is chemical/physical treatment only.




The performance of System 2 is discussed later in this report.

-------





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-------
                                                                      210
     Table 4 displays the leachate treatment efficiency of the two




operating periods in the System 1 sequence in comparison to the dis-




charge standards.  As seen in this table BOD removal exceeded 99%




during the first operating period but only approached 95% during




the second.  Conversely, ammonia removal during the later period




exceeded 99% while during the earlier period of operation only 89%




ammonia removal was achieved, on the average.  Finally, COD removal




approached 95% during both these operating periods.  No satisfactory




explanation for these variations in performance has been developed.




     Presented in Table 5 are the average costs of operation and




maintenance of this treatment facility in the System 1 sequence.




You will note in this table that power costs account for nearly two-




thirds of the cost of treatment.  This high power cost  reflects the de-




mand for leachate and effluent pumping and maintenance of the laboratory




in 'addition to the requirements for actual treatment.  In this treatment




process, the aeration blowers account for the greater energy consumption.




Labor of approximately 20 man-hours per week is not included in these




costs.  Please note that costs presented in this table are the averages




of data collected only for these two periods of operation.




     Leachate treatment in the System 2 sequence was evaluated over a




longer period of time than by any other sequence.  Since System 1 includes




System 2, information on this chemical/physical treatment sequence was




gathered during the periods of operation in System 1.  In addition,




except during the brief periods of evaluation in the Systems 3 and 4




treatment sequences, evaluation of the treatability of raw leachate by




System 2 was continued.

-------
                                                      211
                   TABLE 5
SYSTEM 1 - OPERATION AND MAINTENANCE COSTS
    (8/1/76 - 5/1/77; 7/1/78 - 8/31/78)
Total Flow, gal               5,953,255

Lime, lb/1000 gal                36.43

Sulfuric acid, gal/1000 gal       0.132

Phosphoric acid, gal/1000 gal     0.019

NaOH, gal/1000 gal                0.123

NaOCl, gal/1000 gal               0.151

Costs, $/1000 gal
     Power                        1.92
     Lime                         1.10
     H2S04                        0.10
     H3?04                        0.05
     NaOH                         0.08
     NaOCl                        0.11
     Total                        3.36

-------
                                                         212
     The System 2 treatment sequence has essentially been evaluated




in three modes.  Since System 2 data gathering began prior to accumulation




of the biomass, some data has been gathered on the effectiveness of




lime addition to the raw leachate followed by clarification.   The




majority of data on this treatment sequence was gathered when the




system included chemical addition, primarily lime, to both assist




in heavy metal removals and clarification, as well as, raise  the




pH to above 10.5 to enable ammonia removal by stripping in the aerated




lagoon.  Data gathering in the final mode followed installation of the aerated




equalization lagoon at the head of the plant.  Leachate, when treated




only in the System 2 sequence, was returned to the landfill.




     In Table 6 is presented the performance data on System 2.   Values




contained in this table are the averages of all samples analyzed.




As indicated, influent values are the averages for the entire project




period.  Lime treatment effluent values are those collected whenever




this process was in operation.  Finally, ammonia stripping lagoon




effluent values are those obtained whenever it was operating.  For




this reason effluent values should   be   compared only to influent




and not  to one another except in a general way.




     The information in Table 6 generally indicates the beneficial




effect of the ammonia stripping lagoon.  As seen, ammonia was reduced




by nearly 60 percent when the lagoon was in operation.




     Presented in Table 7 are the average costs of operation and mainten-




ance of this treatment facility in the System 2 sequence.  As seen in




this table, cost information is presented for three operating periods

-------
              TABLE 7. OPERATION AND MAINTENANCE COSTS - SYSTEM 2 -
                    (11/15/75 - 5/1/77 and 11/1/77 - 8/31/78)
Flow, average gpd
Lime, lb/1000 gal
NaOH, gal/1000 gal
NaOCl, gal/ 1000 gal
Costs, S/1000 gal
Power
Line
NaOH
NaOCl
During Operation Without Lagoon
11/15/75 - 6/14/76
22,805
29.7
0
0

1.48
.89
0
0
During Operation With Lagoon
6/14/76 - 5/1/77 &
11/1/77 - 8/31/78
38,618
19.40
0.044
0.054

] .70
0.58
.03
.04
Total
                                    2.37
                                                                     2.35
               TABLE 8.   SUMMARY  OF  SYSTEMS  3  AND  4  (5/1/77  -  8/31/77)
Parameter
Alkalinity
Ammonia-N
BOD5
Cadmium
Calcium
Chloride
Chromium
COD
Copper
Dis. Solids
Hardness

Kjeldahl-N
Lead
Magnesium
Mercury
Nickel
Phosphates
Potassium

Sul fate
Sus . So] ids
Zinc
* No d i ',„' h irg
x Average C.T
Raw
Leachate
x(mg/l)
5087
649
12649
0.11
937
4178
0.48
21152
0.27
14742
4463
348
708
0.76
350
0.007
2.0
2.3
1076
1536
658
1136
40
;i- standard for
u'euLra t i cm .
System 4
Effluent
R(mg/l)
2788
312
2150
0.08
573
3778
0.37
4680
0.22
10081
2805
195
347
0.50
242
.007
1.29
4.6
996
1412
853
1322
19
R(%)
45.2
51.9
83.0
27.3
38.8
9.6
22.9
77.9
18.5
31.6
37.1
44.0
51.0
34.2
30.9
0
35.5
7.4
8.1
—
—
52.5
System 3
Effluent
X(mg/l)
1178
153
763
0.02
287
1496
0.08
2257
.07
5353
924
1.02
180
0.15
48
.002
0.27
0.56
476
719
513
180
0.51
R(%)
76.8
76.4
94.0
81.8
69.4
64.2
83.3
89.3
74.1
63.7
79. 3

7 4 . 6
80.3
86.3
71.4
86.5
75.7
55.8
53. 2
22.0
84.2
98 . 7
Discharge
Standard
(mg/1)
*
35
100
0.02
5V
*
0.1
*
0. 2
*


0.1
0.01
*
*



0.6
this parameter.
R Percentage r
enoval .




-------
                                                                    214
one without and two with the ammonia stripping lagoon in operation.




As with System I power costs represent the major cost of leachate treat-




ment.  Because of fluctuations in the raw leachate quality and the




fact that the operating periods do not overlap,  the two total cost




figures should not be directly compared.




     Following completion of the intitial evaluation of System 1 on




May 1, 1977, a four—month evaluation of treatment sequences, Systems 3




and 4, was conducted.  System 3 consisted of reversing the flow so that




raw leachate first entered the biological treatment tanks followed by




chemical/physical polishing of the effluent.  System 4 represents the




treatment efficiencies of the biological treatment section alone.  These




two treatment sequences were attempted only after the activated sludge




had become acclimated to leachate, since early project attempts to




acclimate a sewage activated sludge  to raw leachate had failed.  Table




8 summarizes the efficiencies of these two sequences in treating land-




fill leachate.




     As seen in this table biological  tieatment only, while showing




significant reductions in organic matter, did not perform anywhere




well enough to permit discharge in compliance with the facilities dis-




charge permit.  System 3, which included, chemical/physical polishing




of the effluent, achieved significantly greater removal efficiencies but




again failed to reach discharge  standards.  No cost information was




developed for these treatment sequences.




     The overall conclusion, based upon system performance in the four




described  sequences, is that treatment of leachate from this landfill

-------
                                                                   215
must include biological treatment preceded by chemical/physical processes.





     Of the several additional leachate treatment technologies investigated




in bench-scale units on a limited basis, only activated carbon filtration




and breakpoint ch]orination yielded meaningful results.  Carbon filtra-




tion of this raw leachate was unsuccessful due to rapid plugging of




the filter media.  Carbon filtration of system effluent  however,




provided significant additional reductions in heavy metal concentrations.




Breakpoint chlorination was demonstrated as accomplishing additional




ammonia reduction in the final treatment plant effluent.   The remaining




limited evaluations of methods for improved heavy metals and suspended




solids removal were inconclusive.




     A more complete discussion of these bench-scale evaluations, as well




as  a thorough discussion of performance in the Systems 1 through 4




treatment sequences, is included in the final report on this demonstration.




This report, entitled "Demonstrating Leachate Treatment-Report on a




Full-scale Operating Plant," will be available shortly from the Office




of Solid Waste.

-------
                                                               216
               Leachate Treatment Demonstration
            Discussion Leader:  Mr. Bernard J. Stoll
Question:  Would you please elaborate on the annual precipitation.
Answer:    The rainfall is about 150 centimeters per year.  Infiltration
           is estimated at about half of that; in other words half is
           run-off and half infiltrates.
Question:  In the United States, chemical  treatment is used first, fol-
           lowed by biological; in Japan,  biological treatment is used
           first, followed by chemical treatment.  Would you please
           comment on this.
Answer:    At this landfill with this leachate, the very high ammonia
           concentrations, the interfering metals and the very high
           organic content prevented establishment of the biological
           mass to treat it—without first treating it chemically.
Question:  In Japan we started out with the same idea.  We used chemical
           treatment first followed by biological.  But we found out
           later on that having biological treatment first is more
           economical; that's why we switched our treatment.
Comment:   At this particular facility when we tried biological first
           followed by chemical, we did not get as good results.  There-
           fore, it would not be as efficient at this facility.

-------
                                                    217
2.   Leachate Control and Treatment
    Leachate Treatment at  Solid Wastes  Disposal  Site
                           By
                  Tadayuki Morishita
        Director of Waste Management Division,
 Water Supply and Environmental Sanitation Department,
             Environmental Health Bureau,
             Ministry of Health $ Welfare

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                               Contents

                                                                 Page
1.  Basic Conception on Treatment 	   1
2.  Scope of Leachate to be Treated 	   1
3.  Treatment Standards 	   2
4.  Treatment Capacity 	   2
4.1  General 	   2
4.2  Remarks 	   3
5.  Leachate Quality 	   5
5.1  General 	   5
5.2  BOD 	  6
5.3  SS	  6
5.4  pH	  7
5.5  Number of Bacillus Coli 	  7
5.6  Heavy Metals 	  8
5.7  Conditioning Pond 	  8
5.8  Remarks 	  8
6.  Treatment System 	  9
6.1  General 	  9
6.2  Sludge Treatment 	 10
7.  Installation of Leachate Treatment Facility 	 12

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                                                               219
             LEACHATE TREATMENT AT  SOLID WASTES DISPOSAL SITE


 1.  Basic  Conception on Treatment
    Treatment  facilities  shall have a capacity to treat leachate dis-
    charging from  a disposal site  to assure that it does not contaminate
    neighboring public waters or ground water.
    However, as leachate oozes out  through damped layers of solid wastes
    in disposal sites, wastes or decomposed products will be dissolved
    into leachate.
    Therefore, leachate generally  contains BOD, COD and SS of high con-
    centration, though it varies with the kind of wastes and structure
                                 *
    of disposal sites.
    The Law  on Wastes Treatment & Cleaning prohibits in Article 2, para-
    graph 8  the installation of any disposal sites not conforming to
    such technical standards as stipulated in the Order of the Prime
    Minister's Office and the Ministry of Health and Welfare, No. 1
    (hereafter referred to as "The Technical Standards").   Pursuant to
    this stipulation,  the Technical Standards stipulate in Article 1,
    paragraph 5 measures to prevent leachate in disposal sites from
    contaminating neighboring public waters or ground water.
    As mentioned,  there are legal and environmental constraints against
    discharge of leachate and,  accordingly, leachate treatment facili-
    ties must have a capability to  treat leachate to an extent where
    these legal and environmental requirements are satisfied.

2.   Scope of Leachate  to  be Treated
    Scope of leachate  to  be treated shall in principle  be  leachate  from
    wastes  or decomposed  products thereof.   In determining the  scope of
    leachate to be  treated,  consideration shall be  given to  the fol-
    lowings;
                                -  1 -

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                                                              220
    (1) leachate collection method, and
    (2) sudden increase in leachate as a result of rainfall.

3.  Treatment Standards
    Leachate shall in principle be treated in accordance with the Ef-
    fluent Treatment Standards stipulated in the Order of the Prime
    Minister's Office, and if necessary, with the following require-
    ments ;
    (1) other effluent standards enforced in the area where leachate
        is discharged, and
    (2) status on utilization of water in the area where leachate is
        discharged.

4.  Treatment Capacity
4.1  General
     Treatment capacity shall be determined in consideration of the
     following factors.
     (1)  Quantity to be treated
         For determining quantity of leachate to be treated, a rational
         formula shall in principle be employed for average quantity
         and the experimental formula for maximum quantity.  In this
         instance,  it is preferable to combine either of these formula
         with others to verify its objective validity.
     (2)  Capacity of treatment facilities
         The capacity of treatment facilities shall be determined in
         consideration of maximum and average quantity of leachate.
                                - 2 -

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                                                                      221
     (3) Conditioning pond capacity
         The conditioning pond (including other facilities having
         similar functions) shall in principle have a capacity enough
         to accomodate sudden increase in quantity of leachate, except
         when there is a likelihood of water contamination judging from
         the property of leachate or specific condition of an area
         where leachate is discharged.
4.2  Remarks
     In determining quantity of leachate, it is essential to learn why
     and how it is generated.
     It is assumed that leachate is derived from 1)  rainfall on a
     disposal site, 2)  water contained in wastes and 3)  infiltration
     of surface and underground water into the disposal  site.   Of
     these, infiltration of surface or underground water can be pre-
     vented by impermeable walls or rain water collector.   Likewise,
     water contained in the wastes does not pose a serious problem
     as it does not produce much leachate.  Predominantly, rainfall
     on the disposal sites is a primary factor for generation of
     leachate.
     Measurement of generation of leachate at  various disposal sites
     provide the following results;
     1) In the event of a relatively heavy rainfall,  leachate quantity
        reaches a peak  with a time lag after rainfall and  it decreases
        suddenly in 2 - 3 days,  but the effect of rainfall remains for
        sometime thereafter.
     2) In the event of steady rainfall without particular peak of
        intensity,  leachate quantity tends to  increase gradually and
        decrease slowly thereafter.
                                -  3 -

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                                                               50?
3) In absence of rainfall for a long time,  leachate quantity
   gradually decreases,  but not to a point  of  being exhausted.
   Therefore, it often occurs that leachate quantity exceeds
   precipitation in following month after a month with  heavy
   rainfall.
   Period during which there remains clear  effect of rain water
   on generation of leachate, though it varies  with disposal site,
   is attributable  to  the degree of compaction in each  site.
   Therefore, in order to stabilize leachate quantity,  careful
   precaution is essential against possible generation  of internal
   water channel.
   From the above,  it  is  learned that leachate quantity relates
   principally to precipitation and that mode  of  occurrence is
   considerably equalized due  to long period of time.   Such back-
   ground accounts  for the propriety for employment  of  the ration-
   al formula which calculates  average quantity of leachate on
   the basis  of average precipitation.  However,  in  the case of
   calculating maximum quantity of leachate, application of the
   rational formula is impracticable because leachate is  generated
   in different manner after rainfall depending on its  intensity,
   and therefore, it is preferable to use the  experimental formula
   representing these  relations.
   Whichever  formula may  be used,  it  is always  desirable  to
   calculate  with other formula as  well for  comparison.

   (T)  Rational formula
       The  rational formula is  given by
      where,
           Q:  Leachate quantity (m3/day)
           C:  Run-off coefficient (m3/m3)
           I:  Rainfall (mm/day)
           A:  Catchment area (m2)

                          - 4 -

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                                                                223
             Experimental formula
             The following formula  experimentally  obtained  at  Fukuoka
             University  is the  most popular.
                  Q  =  10 In [o.'X-Ss+Sa)Kr+(l-A)-Ss/D]l/N
                    Kr = ~  (0.002R2+0.16R+21)
            where,
                 Q:  Leachate quantity  (m3/day)
                 In:  Probable daily rainfall during the n year  (mm/day)
                 a:  Rate of rainwater  infiltration into disposal  site
                 X:  Surface run-off rate
                 Ss:  Catchment area (ha) around disposal site
                 Sa:  Site area (ha)
                 Kr:  Run-off coefficient
                 D:  Average number of days for leachate to reach
                     collector tube from the center of a catchment area
               1/N:  Rainfall frequency
                 R:  Daily rainfall (mm/day)
            In this formula, the term otXSs represents the quantity of
            surface water infiltrating into the disposal site across
            the  rainwater conduits, and the term (1 - X) Ss/D re-
            presents the quantity of ground water infiltrating into
            the disposal site.

5.  Leachate Quality
5.1  General
     Leachate quality shall  be  determined on the basis of water quality
     analysis and test  results  at other  treatment  plants of  the similar
     type,  but in this  connection,  it  should be noted  that comprehensive
     decision should be passed  on the  basis of  studies on (1)  through (3)
                                -  5  -

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                                                                    224
     in view of the fact that the quality of leachate considerably varies
     with the kind of wastes in the disposal site and with the structure
     of the site.
     (1) Kind of pollutants
     (2) Concentration of pollutants
     (3) Aged deterioration of quality
     (4) Determination of leachate quality
     On these premises, basic requirements for separate treatment facil-
     ities for each pollutant and common treatment facilities for various
     pollutants are explained herein under.
5.2  BOD
     In the case of BOD treatment, biological process is popular thanks
     to its efficiency, stability and economy.  In the case of leachate
     treatment, it is preferable to install coagulating and settling
     plants, due to extreme BOD load fluctuations, for the purposes of;
     1) preventing the outflow of activated sludge and biological
        membrane for complete removal of adsorbent BOD,
     2) partial elimination of COD and color, and
     3) strict removal of SS and removal of heavy metal.
     The coagulating and settling equipment shall in principle be
     installed in the downstream process of biological treatment
     facilities for efficient operations in paragraphs 1) and 2).
5.3  SS
     Regarding SS treatment,  it is considered that no particular treat-
     ment facilities are required provided that conditioning ponds have
     a large capacity and are of a structure capable of removing soil
     and bulky SS because a small amount of SS can be treated in the
                                - 6 -

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                                                                225
     biological treatment facilities.  However, in case such condition-
     ing pond is not installed, the capacity of pond is too small,
     there is a likelihood of an abrupt increase in SS as a result of
     increase leachate run-off, or in presence of a plenty of organic
     SS at disposal plants mostly treating kitchen garbages, it is
     essential to install a precipitator in the upstream process so as
     to alleviate load on the biological treatment facilities.
     In absence of the conditioning pond, it is necessary to install
     grit chamber in front-of a regulating tank in order to prevent
     wear of pump and piping afflicted by soil or sand.

5.4  pH
     There is no need of paying particular consideration to pH except
     when kitchen garbages or incinerated ash constitutes wastes in
     the disposal site.  In the case of installing treatment facil-
     ities, it is preferable to install in the upstream of the afore-
     mentioned precipitator if any, considering potential adverse
     effect on biological treatment facilities due to failures or
     accidents.

5.5  Number of Bacillus Coli
     Due to active decomposition activities of microorganism within
     the wastes  in a disposal site, there is a likelihood that bucillus
     coil group  are contained in leachate.   Accordingly,  it is in
     principle necessary to  install chlorinators except when leachate
     is discharged into a sewerage system at the downstream of effluent
     treatment facilities to avoid exerting adverse effect on other
     treatment processes and for perfect and efficient  treatment.
                                -  7  -

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                                                              226
5.6  Heavy Metals
     There is no need of installing particular treating equipment
     because heavy metals are removed in the treatment process for
     other pollutants.

5.7  Conditioning Pond (tank)
     Conditioning pond (tank) plays an important role of storing leachate
     and regulating its quantity to facilitate smooth treatment of
     leachate.  It is in principle recommendable to install this facil-
     ity.  In case the conditioning pond (tank) has a large capacity,
     such tank (including other facilities having similar function)
     is often installed in the disposal site.  However, should this
     result in accumulation of leachate in the wastes layer or water
     collector pipes, there would arise a need to provide a small con-
     ditioning tank in the leachate treatment facilities.   The condition-
     ing tank, which structurally permits easy installation of preliminary
     aeration system, plays an important role as a pretreatment equip-
     ment when processing leachate containing high concentration of BOD
     and soluble iron.

5.8  Remarks
     (1) It is assumed that pollutants contained in leachate are derived
         from 1)  water or soluble elements in wastes, 2)  biologically
         and  chemically and physically decomposed organism contained in
         the  wastes and 3)  materials in covered or neighboring soil.
     (2) BOD, COD and ammonium nitrogen
         As mentioned in paragraph (1),  concentration of  pollutant in
         leachate is basically affected by wastes concerned, but equally
         by the structure of disposal site and method of  burial.

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                                                                 2?7
      (3)  Decomposed  products by microorganism form a major source of
          supply  for  pollutants in  leachate, but as these substances
          change  in the processes of decomposition and self-purification
          function within  the layers of wastes, leachate is subjected to
          peculiar aged deterioration in respect of quality.
      (4)  The quality of leachate is basically affected by type of wastes
          mentioned in paragraphs (1) through (3), but also by the struc-
          ture of a disposal site and the method of burying wastes.
          Leachate quality is also  subjected to considerable aged deterio-
          ration.  Of these, the kind of wastes is considered as a factor
          of designing leachate quality, but regarding aged deterioration,
          attempt has been made to  resolve this problem by modifying the
          design of treatment facilities.  With regard to the structure
          of disposal sites and the method of burial, it is recommendable
          to adopt the following system for easier and more economical
          operations.
         Namely, it  is necessary to install water collection pipes to
         prevent leachate from accumulating in the wastes layers and to
         provide good aeration.   Also,  it is preferable to bury wastes
         into smaller blocks of a given area subdivided from a major
         catchment block in consideration of workability, scale and
         layer thickness.

6.  Treatment System
6.1  General
     The leachate treatment system is based on  the combination of  a
     biological process  and a .coagulating sedimentation  process, but
     tertiary treatment  systems may be  required  depending on  municipal
     regulations and  requirements.
                                -  9  -

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     This, however, is not applicable to a case where there is apparently
     no particular obstacle in prevention of water pollution judging
     from the scale of disposal site, kind of wastes, condition of the
     area in which leachate is discharged.
     Ordinarily, effluent treating facilities are primarily designed to
     remove BOD and SS, but due to a difficulty in stable treatment of
     BOD subjected to extreme load fluctuations, a biological treatment
     process is combined with a coagulating sedimentation process for
     an effective treatment system capable of processing SS, and occa-
     sionally with other unit operation as required.

6.2  Sludge Treatment
     This system comprises sludge concentration tank (including sludge
     storage tank) and dehydrator.
     The concentration tank is designed to trim the volume of sludge
     generated by biological treatment or coagulating sedimentation
     facilities for easier handling,  and should be installed unex-
     ceptionally.
     Dehydrator is required to be installed in case transport distance
     is far, there is a problem in disposal of concentrated sludge or
     there is not  appropriate disposal site in the vicinity.
                               - 10 -

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                                                                                                             229
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                                                                  230
7.   Installation of Leachate Treatment Facility
    Careful consideration shall be given to the following requirements
    in planning to install treatment facilities,  which shall be;
    (1)  designed to treat leachate to comply with the planned quality
        after completion of a disposal site,
    (2)  located conveniently for collection and drainage of  effluent
        and delivery of  equipment and materials,
    (3)  located in a spacious site to allow future  expansion and  provided
        with tertiary treatment plans,
    (4)  designed to provide ease of maintenance and reliable performance
        and comply flexible with load fluctuations,  and
    (5)  the treatment facilities shall  be designed  to harmonize itself
        with neighboring environment and prevent  secondary pollutions.
                               -  12  -

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                                                               231
           Leachate  Treatment at Solid Waste Disposal Site
              Discussion Leader:  Dr. Kentaro Yagome
Question:  With  reference to  leachate quality estimates, your equa-

           tion #1,  Rational  Formula, is essentially that used in

           the U.S.  for estimating surface water run-off in the de-

           sign of run-off control devices; for example, storm sewers,

           highway culverts,  etc.  In estimating leachate generation,

           a  "water  balance"  is frequently performed.  The basic

           equation  is:  Infiltration = Precipitation - Run-off -

           Evapotranspiration.  This infiltration estimate is

           multiplied by the  "catchment area" to estimate volume

           of leachate generated.  Your equation #2, Experimental

           Formula,  seems closer to our approach.  Please elaborate

           on the development of this equation and on the significance

           of its terms.

Answer:    In the Rational Formula $1, "I" is the annual averate of

           rainfall; "C" is equal to 1.2.  More details about this

           computation are included in the paper I just presented.

Question:  With reference to model leachate treatment system design,

           your system includes leachate storage (within the landfill)

           to reduce suspended solids.  Please describe.

Answer:    In Japan,  as a general practice we don't have leachate stored

           within the landfill.   If the geological  configuration requires

           it sometimes we have  to set leachate storage tanks outside

           the landfill.

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                                                            232
Question:  Preferred landfill design in the United States involves




           continuous removal of leachate from the landfill in order




           to minimize the amount of leachate available to leak through




           the bottom liner.  Your opinion on this concept, please.




Answer:    In Japan, in principle,  we don't have actual bottom liners.  In-




           stead we use a strainer—a porous-type strainer and gravel.




Question:  Please explain the operation of performance of the "conditioning




           tank."




Answer:    The conditioning tank is set up so we can do a 24-hour, round-




           the-clock operation.   Additional information is in the paper.



Question:  Since the leachate treatment system is to be designed for




           both current quality, as well as planned quality after com-




           pletion of a disposal site, how do you predict  leachate




           quality?  Do you predict decreasing leachate quality (strength)




           over time?




Answer:    Our estimate is based on actual data concerning four elements




           that I mentioned:  kind of pollutants, concentration of pollutants,




           age deterioration of quality and determination of leachate quality.



Question:  How do you incorporate changing leachate quality in your




           leachate treatment system designs?




Answer:    In Japan, actual data varies between 2 times and 1/5 of the design.




           In order to cope with this fluctuation of quality, we set two




           treatment systems in parallel.




Question:  You periodically refer to "effluent standards."  Are effluent




           standards established on a site-specific basis?  Are effluent




           standards specific to leachate or to any waste water?  How




           are effluent standards implemented?

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                                                                   233
Answer:    It's all controlled by our Water Pollution Control Act.  It is




           under the jurisdiction of that legislation.   The water quality




           from the treatment facilties is subject to inspection; however,




           because general effluent standards for general waste are not




           tough,  most leachate meet the standard.




Comment:   The United States' control mechanism is the Clean Water Act.




           An earlier act by the same title formerly required a case-by-




           case evaluation for a discharge into a stream, based upon the




           quality of the other stream.  Now effluent guidelines are




           being developed for specific waste waters.  We look at the




           quality of the waste water and its impact on most streams or




           how much can be handled by a stream.  But it is not location




           specific now; it is industry specific.  Leachate has not yet




           been addressed so there is no real standard for leachate.




           There are about three facilities in the country where leachate




           standards,  or effluent standards,  have been applied.  The




           Tullytown project mentioned in my report is one of them.




           That is the most lenient.  All of the others are more stringent



           than that.




Comment:   In Japan, in general,  waste water has to meet effluent standards.




           But some localities  have more stringent requirements.   So in




           these areas,  facilities must meet  higher standards.   In these




           cases,  the  operational costs,  as you can imagine,  are increased.

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                                                      234
4,  Resource Recovery Technologies
        4-1  Recycling of Municipal Wastes  in Japan
                            by

                    Tadayuki iVorishita
          Director of Waste Management Division
          Water Supply and Environmental Sanitation Department
          Environmental Health Bureau
          Ministry of Health and Welfare

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                                                                 235
                           CONTENTS










                                                                  Page




     IfrOYlOT'Sl 1      «— _•._ ^ _•_•_     ...    .—-^  _*_•«      -•_ •_  _       1
  •   VJC-IIC i. CLX   •••—^•W— .^^—K_ ^•••V.^MC^^^^BMn. ^___ _»«»___ «b^«»B«^-M. — IW^*-^^^v.*_ _ -_^«...   _^








2.   Surroundings  	   1







3.   Type of  Recycling  	   2





     3-1  Exchange and Bazaar of Disused Articles  	   2




     3-2  Group  Collection by Residents  	   3





     3-3  Recovery of Materials from Municipal ¥astes  	   3










     3-5  Heat RecJovery from Incineration Plants   	   4
4.   Appendix  	

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                                                                236

1 .  General
         The Ministry of Health and ¥elfare set up in 1977 a special committee
    to study recycling of municipal wastes.  The committee conducted a question-
    naire survey of cities and inter-municipal public agency regarding their
    recycling of municipal wastes.  According to the survey, 55.3$ of cities
    and inter-municipal public agency in Japan make recycling of municipal
    wastes by means of source segregation and heat recovery from incineration
    plants, etc.  An outline of the questionary survey is as follows.


       The means of recycling employed by the cities include exchange and
       bazaar of disused articles, group collection of valuables by residents,
       recovery of- materials from collected wastes and heat recovery from
       incineration -plants.

       The popular ways of recycling of municipal wastes by inter-municipal
       public agency inciude recovery of materials from collected wastes and
       heat recovery from incineration plants.


2 .  Surroundings
         The purpose and motive varies with the type of recycling.

       Type of recycling                     Major Purposes
    Exchange and bazaar of disused      Conservation of energy and resources
    articles                            (63.7#)
    Group collection by residents       Reduction of wastes (62. 9$)
    Recovery of materials from          Reduction of wastes (73.2?o)
    collected wastes
    Heat recovery from incineration     Conservation of resources and energy
    plants                              (62. 4£)
    (Parenthesized figures denote the percentages in the cities making
     recycling of each type.)

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                                                                         237

        Problems  of recycling of  vastes  include:
             Difficulty in the  source  separation                 58.2  %
             Expensiveness of extraction and  separation  cost     45.9  $
             Instability of the reclamated  resources  market      38.6  %

        Cooperation of  residents  was cited  by the  greatest number  of  cities
        (87.3$) as  an essential condition for recycling.

        "Promotion  of publicity and education" was cited by the  most  number
        of  cities  (72.6$)  as  the  effective  administrative measures for promo-
        tion  of recycling  of  wastes, followed by "imposition of  deposits and
        cooperation-from industries for  recovery"  (43.6%), "preparation of
        the model project  of  recycling"  (35.8$) and "need of communication
        among cities  undertaken of domestic wastes and other manufacturing
        industries"  (32.7$).
                                         )
        The number  of cities  carrying out recycling of domestic wastes has
        sharply increased  since 1970.  Particularly since the oil crisis,
        there have  been  increased such types  of recycling as "recovery of
        materials from collected wastes", "group collection by residents"
        and "exchange and bazaar of disused articles".

3.  Type of Recycling

    3-1  Exchange and Bazaar of Disused Articles
         "Exchange and  bazaar of  disused articles" is conducted by 102 cities
         (17.8  $ of all respondents escluding inter-municipal public agency.
         This activity  is grouped into two  types:   "exchange of information"
         and  "exchange  and bazaar of disused  articles".   The former is often
                                     -  2  -

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                                                                     138






     conducted by the authorities of the cities, while the latter is




     often conducted by women's associations as part of their voluntary




     ac tivities.









3-2  Group Collection by Residents







     Group collection by residents has sharply increased since 1975.  Of




     574 cities,  119 or 20.7 % conduct group collection.  This is actually




     conducted mostly by local organizations such as community associa-




     tions and by women's associations, children's associations and PTA.









3-3  Recovery of  Materials from Municipal Wastes







     Recovery of  materials from municipal wastes is conducted by 145




     cities,  or 25.3 % of the 574 cities surveyed, and by 59 inter-




     municipal public agency or^27.1 % of the 218 inter-municipal




     public agency surveyed.









     Recovery of  materials from collected waste is conducted as follows:




     Source separation of resources  - sorting out of valuables only




     at waste discharging points by  residents.




     Recovery at  the wastes  disposal facilities - recovery of valuables




     from incombustible wastes by using the  conveyorized manual sorting




     system or fully mechanized system.




     Recovery at  the landfilling site - permitting the  resources




     reclaiming companies to  enter the  landfilling site in order  to




     collect  valuables from  the wastes  there.
                                -  3  -

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                                                                 239






3-4  Composting





     Composting was conducted in various parts of Japan in the early




     1960's, but it decreased sharply due to increase of unsuitable




     component in wastes (e.g. increase of plastic materials) and change




     in preference of farmers (e.g. greater reliance on chemical




     fertilizers).  At present only 8 cities are operating composting




     plants.  Recently, however, the demand for compost is increasing




     because of the worsening fertility of soil.









3-5  Heat Recovery from Incineration Plants





     The waste combustion heat is utilized at 100 cities,  or 17.3 % of




     the total, and by 46 inter-municipal public agency or 21.1 % of




     the total.  It is utili2ed for hot water supply and air condition-




     ing at incineration plants concerned,  for hot water to swimming




     pools and baths at public welfare facilities and for  electric power




     generation.   Electricity thus generated is mostly used at the




     facilities concerned,  and there are only a few cases  of it being




     sold outside.
                               - 4 -

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                                                                   240
4.   Appendix




                       Recycling of Municipal Waste

         - from mail survey by the Ministry of Health and Welfare -



    Total respondents


         No. of the cities  	  574

         No. of the inter-municipal public agencies  	  218
             (vhich include cities)

    Type of the recycling by starting period.
Type of recycling
Exchange or bazaar
of disused materials
Group collection of
valuables by resi-
dents
Resource recovery
from waste
Composting

before
'65
1
15
5
3

'65-
'67
0
£
2
3
3
Period of
'68- '70-
'69 '71
1 3
3 5
11 20

Start
'72-
'73
15
13
43


'74-
'75
50
22
75


'76-
31
52
46
2

NA Total
2 103
8 120
1 204
8
Utilization of
 combustion heat         8    14    15    31    28    34    15     1    146
                                   - 5 -

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                                                                      241


                 Exchange  or Bazaar of Disused Materials

  No.  of the  cities                          102 (17.8$ of respondent cities)

  No.  of the  inter-municipal public agencies  1 (0.5% of respondent agencies)


  Type of conducting organization.
Conducting organization
Municipal authorities
Community association
Vomen ' s association
Children's association
Miscellaneous
NA
No. of
cities
56
4
34
2
40
4
No. of
zation A
57(1) 3
6(1)
111(1) 5
8
91(1) 4
4
T
B
44
2(1)
6

10

y
c
8
i
21
2
22

P e
D
6(1)
1
KD

2(1)


NA
1

1

4
4
        Note:   Types of exchanging methods are as  follows:
              A. Making daily exchanging center or  sales  shop
              B. Delivery of information of disused materials

              C. Exchange party or bazaar on special days

              D. Miscellaneous
  Frequency of exchange or bazaar
 Frequency
No. of Municipal Community Women's Children's Misce-
groups author-     ass.      ass.     ass.    llaneous NA
       ities
Daily
More than once
50
4
42
3
2 1
1
4
 a month

More than fourth    7
 a year

Less than fourth  209
 a year
NA
 11
         11
91
20
81
                                  - 6 -

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                                                                242
Supporting fund from municipal body
                                                               ( unit: yen  )
  Amount of fund
          (yen)
Less than   10 - 20  20-50  50-1  More than
10 thousand thousand thousand million 1 million
                                 Total
 No. of the cities
  that expend the
  supporting fund
                                                    19
Effect
   No. of exchange
 . No.  of
  organization
    Sales                   No. of
    volume   ( yen )     organization
   Less than 500
      52
Less than 10 thousand
 8
   Less than
    500 - 1,000
                 Less than
                 10 - 50 thousand
                              18
   Less than
    1,000 - 2,000


   More than 2,000


   NA
      15

      55
Less than
50-1 million


More than 1 million


NA
 9

 9

96
                                    - 7 -

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                                                                       243
                 Group Collection of Valuables by Residents






No. of the cities   	  119  (20.7




No. of the inter-municipal corporations  	   2  ( 0.9






Conducting organization
Type of organization
Community association
¥omen ' s association
PTA
Children's association
Miscellaneous
NA
No. of
cities
80
55
52
49
23
4
No. of
organization
2,978
685
696
1,739
285
4
Kinds of materials for collection
Kinds of materials
Paper
Textile
Bottles and glass
Metal
Miscellaneous
NA
No. of cities
88
77
81
75
18
22
                                   -  8  -

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Promoting activities by municipal authorities
        Type of activity                      No. of city


 No promoting activity                            23

 Assist by municipal officials                    29

 Assist to PR                                     68

 Supporting fund                                  25

 Permission of use of public space for             9
    recycling activity

 Miscellaneous                                    15
                                - 9 -

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                                                                   245
                      Recovery of Materials  from Waste
No. of the inter-municipal
Type of waste for resource reco
Type
Bulky vaste
Mixed vaste
Combustible vaste
Incombustible vaste
Resource vaste
(Source separated rich
in resources)
Miscellaneous

very
No. of the No. of the
... . 1 ot/a.4.
cities agencies
71 25 96
8 8
11 2 13
102 38 140
28 10 38
112
Effect of vaste reduction
   (to the fraction of the vaste)
Rate of j.
Type Reduction -5% KW
of recovery '"
method
Fully
Manual
Manual
NA
mechanized process 12 14
vith conveyer system 4
27 14

20$ 50fo 80% NA
15 7 5
4 13 74
11 11 85
9
                                  - 10 -

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                                                       246
4.  Resource Recovery Technologies
  4-1  Recycling of Municipal Waste in Japan (2)
                            By
                    Tadayuki Morishita
          Director of Waste Management Division,
   Water Supply and Environmental Sanitation Department,
               Environmental Health Bureau,
               Ministry of Health § Welfare

-------
                                                                247
                              Contents

                                                                Page
1.  Used Paper 	   1
1-1  Present Situation of Recycling 	   1
1-2  Recovery Ratio 	   1
1-3  Origination of Used Paper and Flow of Recovery 	   3
1-4  Measures to Promote Recycling 	   5
1-4-1  Upbringing of Collectors 	   5
1-4-2  Stabilization of Supply and Demand 	   5
1-4-3  Selection of Used Paper from Municipal Waste 	   5
1-4-4  Development of Techniques for Recycling of Used Paper ..   5
2.  Recycling of Scrap Iron 	   6
2-1  Steel Production and Scrap Iron Utilization 	   6
2-2  Distribution System	   6
2-3  Measures to Step Up Recycling of Scrap Iron	   8

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                                                             248
           4-1  RECYCLING OF MUNICIPAL WASTE IN JAPAN (2)
1.  Used Paper
1-1  Present Situation or Recycling
     The quantity of used paper consumed for paper production in Japan
     in 1975 stood at 5.24 million tons, accounting for 36 percent of
     all materials for paper production.
     The consumption of used paper since 1965 is indicated in Table 1.

             Table 1  Changes in Consumption of Materials
                      for Paper Production
       Source:  Paper Recycling Promotion Center..   ,      ,     N
                  r      76                 (ln thousand tons)
Year
1965
1970
1973
1974
1975
1976
1977
Pulp
4,975 60%
8,877 64
10,438 62
10,335 63
9,040 63
9,947 61
10,015 60
Used paper
2,847 35%
4,696 34
6,343 37
5,866 36
5,235 36
6,331 39
6,625 40
Others
418 5%
228 2
150 1
149 1
91 1
58 0
51 0
Total
8,240 100%
13,801 100
16,931 100
16,350 100
14,366 100
16,336 100
16,691 100
1—2  Recovery Ratio
     The recovery of used paper has reached 40 percent in Japan.
     Changes in the recovery ratio are shown in Table 2, whereas
     the recovery ratio by type of commodity in 1977 is shown in
     Table 3.

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                                                                 249
          Table 2  Changes in Recovery Ratio  of Used  Paper




     Source:  Paper Recylcing Promotion Center
                                                (in  thousand  tons)
Year
1965
1970
1973
1974
1975
1976
1977
Paper supplied
7,108
12,260
15,802
14,576
13,338
14,874
15,341
Used paper
recovered
2,725
4,732
6,281
6,010
5,162
6,178
6,602
Recovery of used
paper in ratio
38%
39
40
41
39
42
43
          Table 3  Recovery Ratio by Type of Commodity




Source:  Paper Recycling Promotion Center
                                                 (in thousand tons)
Type of commodity
Best white shavings, white
card
White woody shavings,
white manila
Fine paper print (includs
corted paper)
Quires woody paper printed
Old magazines
Old newspaper
Craft browns
Old corrugated containers
Box board cuttings,
mixed paper
Total
Used paper
recovered
in Japan
91
59
734
145
586
1,518
144
2,961
364
6,602
Paper and card-
boards consumed
in Japan

• 6,293
2,211
697
4,602
1,538
15,341
Recovery
Ratio

f25.7
68.7
20.7
64.3
23.7
43.0
                               - 2 -

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                                                                     250
1-3  Origination of Used Paper and Flow of  Recovery
     The types of used paper include,  among others,  used  industrial
     paper which come from enterprises and  other  big sources  of
     origin, and used municipal paper  which comes from  households
     and small stores.  The channel of recovery is complicated as
     shown in Fig. 1.  In the long run, used paper is delivered  by
     direct-delivery agents.

-------
                                                                                                         251
3
>,
o

3.
S
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             b
             «
             O. a
             « -a
             O. b
               a

             •ss
                                                             (WE1?)    T09'9

                                                         jatlt'd pasn jo  Aj-jAOO
B.
a
a
                     u -a


                     I"
                     5 o
                      7\»!
         •a o.
         3 1-1
         • ->  wa o
         u o  o.u o
         b a  o

                                                                                                         3

                                                                                                         ^3
                                                                                                         •H
                                                                                                         V)
                                                                                                         4J

                                                                                                         
-------
                                                                       252
1-4  Measures to Promote Recycling
1-4-1  Upbringing of Collectors
       In the system of collection of used paper, it is said that
       there are about 40,000 collectors of used paper at the
       terminals, such as those engaged in exchanging used paper
       with toilet paper, purchasers and collectors.  Their business
       is unexceptionally small in scale, and there is a need to
       bring up and strengthen them.

1-4-2  Stabilization of Supply and Demand
       The supply and demand of used paper are influenced by a rise
       or fall of the paper production industry.  Alos depending on
       it, the prices also repeatedly fluctuate.  To cope with this
       situation, Paper Recycling Promotion Center is engaged in
       stocking used paper, but it is necessary to strengthen and
       expand this organization.

1-4-3  Selection of Used Paper from Municipal Waste
       For the selection of use paper from municipal waste, air-
       classification, semi-wet type separation and other techniques
       have been developed, so it would be of more effect, should a
       subsystem for the selection of used paper be incorporated, if
       possible at all judging from relations with users, in the
       municipal waste processing system.

1-4-4  Development of Techniques for Recycling of Used Paper
       In the conventional used paper recycling process, its use is
       limited in view of deinking.
       It is necessary, therefore, to encourage the recycling by
       developing techniques in this sector.
                                 - 5 -

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                                                                253
2.  Recycling of Scrap Iron
2-1  Steel Production and Scrap Iron Utilization
     The consumption of pig and scrap iron for steel production in
     Japan in 1975 stood at 89.23 million (metric) tons and 37.90
     million tons (including cast iron), totaling 127.13 million tons
     and suggesting that iron scrap accounted for 30 percent of the
     materials for steel production.
     Of these iron scrap, 18.11 million tons were recycled from
     various manufacturing industries (excluding steel mills), dis-
     carded automobiles and general households and 17.40 million
     tons from steel mills, and 2.39 million tons was imported.  Of
     the 18.11 million tons, 0.62 million tons was recycled from
     discarded automobiles and general households.
     Imported scrap iron accounted for a little over siz percent,
     four-fifths coming from the United States.

2-2  Distribution System
     The figure shows the scrap iron distribution system in Japan in
     1975.  Of the 18.11 million tons of scrap iron recycled from
     manufacturing plants (excluding those for steel production),
     discarded automobiles and general households, 20 percent was
     directly delivered to steel manufacturers by way of major firms
     engaged in direct delivery, whereas some went to the firms
     engaged exclusively in the processing of scrap iron.  And fifty
     percent was delivered through trading houses or wholesale houses
     to steel manufacturers by medium-sized, delivery firms as it
     was (i.e., unprocessed) or by processing firms after processing.
     The remaining 30 percent was collected by small-sized collecting
     agents and processed by terminal collection centers known as
     "Tateba" for chaneling in the distribution system.

-------
                                                                                            254
                                                                                    (in million tons)
    Blase
    furnace
    makers
   Open-
   he arch
   electric
   furnace
       U.S.
                  Others
               Machinery, electric, vehicle,1
               shipbuilding and other
               plants, and offices
  Discarded auto-
  mobiles and general
  households
   <75Z)
(25Z)

(802)
(202)
              17.90
          Own waste
S!
                                      2.39
                              Imported waste
           z&
          "1"
          sic
          0 « O
          a. co -H
          • tt w
          •M .rt O
          •O -O OJ
                                HUM
                                S'H C
                    • a a
                    « « «
                    U ag u
                    832
                    C ~ a
                                                    (66%)
                                                   Collected domestic
                                                   and urban waste
                                        (202)
                                          r
                                                    (50%)
                                                           (302)
                                                                                 Collection agents
                                                           Medium-sized
                                                           delivery agents
                                                                   Tateba  (terminal
                                                                   collection centers)
                                             Major delivery
                                             agents (direct
                                             delivery agents)
                                          i
                           Trading houses
                                      asz
                                       •V-20Z)
                                                                               Scrap  iron processing
                                                                               agents
                                          Trading houses
                                                     ...(60V7pZl.t
                                                          Wholesale houses
                                                          (slips only)
     (25Z)
           (62Z)
                                                                   (15120%)  t
                                               37.90
                     (11Z)
                          (1-6Z)
(O.AZ)
     Blast furnace
     makers
         Open-hearth
         electric furnace
         makers
                  Pig  iron and
                  cast  iron makers
                         Rerolled steel
                         makers
    Others
                               Scrap  Iron Distribution System

     Note:   Source;  Ministry of  International Trade  and Industry

-------
                                                                    255
     Thus, the distribution system of scrap iron is complicated,
     with the consequence that the distribution cost increases and
     unfavorable influences are produced on steel production and the
     scrap iron industry.
     The unit price of scrap iron markedly fluctuates.  The unit
     purchasing price fluctuated from ¥25,000 in July 1973 to
     ¥46,000 in November 1974.

2-3  Measures to Step Up Recycling of Scrap Iron
     (1)  Strengthed Recycling of Scrap Iron from Waste from
          Municipalities
          Provided that the amount of metals in household waste is
          six percent, of which iron accounts for four percent, it
          may be surmised that the 28 million tons of waste (includ-
          ing bulky refuse) included more than 1.1 million tons of
          scrap iron.  Its recycling will be strengthened.

     (2)  The collection of scrap iron from automobiles which are
          discarded but not collected will be strengthened.

     (3)  The system for the distribution of scrap iron will be
          streamlined to decrease the distribution cost and a stock-
          ing system in the distribution mechanism will also be
          strengthened to minimize fluctuations in price.

-------
                                                                    256
               Recycling of Municipal Waste in Japan
               Discussion Leader:  Dr. Masaru Tanaka
Question:  You mentioned that you will respond to homeowner calls for

           newspaper pick ups.  How can that be profitable?  Don't you

           have regular pick-ups?

Answer:    I believe that the pick-up was mentioned with regard to recycling

           bottles.  In Japan, for example, you can telephone a beer retailer

           and he will deliver bottles of beer to your home.  He then picks

           up your empty bottles and returns them to his store.

Question:  "Promotion and education" was cited by most municipal authorities

           as the most effective administrative measure for promoting mater-

           ials recovery.  Could you please describe the publicity measures

           that have been the most effective in motivating citizen partici-

           pation and those that have been the least effective?

Answer:    Our information is based on information from the localities—it

           is not ours.  I imagine that the most effective publicity

           technique would be for local administrators to attend meetings—

           township and regional meetings—promoting the idea of resource

           recovery.  Another effective measure would be the posting of

           posters promoting  resource recovery.

Question:  The two biggest problems of recycling were listed as "difficulties

           in the source separation" and "expensiveness of the extraction

           and separation cost."  Could you please elaborate on these two

           and explain what is done to lessen them?

Answer:    The reason we cited the difficulties in source separation is

           because we separate waste into several types—combustible,

-------
                                                                    257
           hazardous,  recyclable.  In  order  to accomplish  this  type  of




           separation, we have  to  train people.  It  takes  time and money




           to  train people and  ensure  good execution.  I'd like  to share




           my personal experience  with source separation which  illustrates




           your problems.  I live  six  miles  outside  of Tokyo.  In my




           area,  the waste that  is unfit for combustion is collected




           every Monday.  The waste  that can be combusted  is collected




           Tuesday, Thursday and Saturday.   We have  to label the waste




           that is being collected.  Each family has two different




           trash cans; one is for  combustibles and the other is for




           non-combustibles.  If you make a  mistake and mix the waste,




           collectors  will leave it uncollected.  So, this is part of




           Japanese psychology.  It  is sort  of embarrassing to separate




           waste and then make a mistake.  Everybody knows when your




           waste is not collected and  it embarasses  the individual.




Question:  The Monday  pick up for  the  non-combustible garbage is municipal,




           as I understand it.  Who then makes the Tuesday, Thursday and




           Saturday pick up and for what purpose?



Answer:    The municipal agency picks up the combustible garbage on  Monday.




           Then on Tuesday,  Thursday and Saturday, the non-combustible




           garbage is picked up by the municipality and placed in the




           landfill.




Question:  Then all of these collections are made by the municipality?




           There are no private collectors?




Answer:    Yes, the municipal government handles 80% of the waste collection.




           The remaining 20% is picked up by private collectors.  Last year,

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                                                                 258
           we conducted some surveys of cities surrounding Tokyo and




           found that most cities provide as many as four labeled—




           specifically labeled—garbage and trash cans per household.




           For example, they might be labeled: bottles, papers, rags.




           The cities provide these trash cans to homeowners and it is




           working well. Kawasaki City is ^eady to implement this system




           and if it is successful, it may lead to rr
-------
                                                                          259
Question:  Most of the collection systems cited had separate collections




           of glass and metals but not paper.  If this true of all




           collection systems or is paper recovery primarily handled




           by the private sector?




Answer:    Here we are talking about only source separation of paper,




           glass and metal.  For source separation, we recover paper, glass




           and metal but from the combined or mixed waste collection we don't




           recover metal.




Question:  It has been reported to the United States by the United Paper




           Institute that there may be a capital expansion in Japan to




           build a new paper mill that will be dedicated to the use not




           of virgin pulp, but of recylced paper.  Since Japan enjoys




           one of the highest recycling rates in the world, one assumes




           that much of this paper could be expected to come from the




           United States.  Do you have any dates as to when this might




           happen and do you have any idea how much this chart might




           rise as a result?




Answer:    So far we have several plants that use only recycled paper.




           We don't have any information that there will be a new plant;




           so we cannot answer your question.

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                                        26O
4-2  AN EFFECTIVE USE OF WASTE HEAT

     OF REFUSE INCINERATION


  -THE EXPERIENCE OF SAPPORO CITY-
                by
FUJIO OIKAWA
  Director of Public Cleansing Dept.
  Environmental Bureau of Sapporo City

HIROTO MITANI
  Chief of ATSUBETSU Incinerator Plant
  of Public Cleansing Dept.
  Environmental Bureau of Sapporo City

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                                                                  261
                                 CONTENTS


                                                                      page

 1 .  Introduction .................................................



 2.  Refuse disposal abstract in Sapporo .........................      2

    2-1   Topography  and countermeasure of  Sapporo ..... . ........      2

    2-2   The collection  and disposal of waste  refuse .............      3

    2-3   The quantity  and composition  changes  of  refuse ..........      5



 3.  Refuse  Incinerator and the use of  waste  heat .................      9

    3-1   Continuous municipal incinerator ........................       9

    3-2   The use of waste heat from  incinerator plant ...........       ^



 4.  District Heating using waste  recovering heat .................      1£

    4-1   Abstract ..............................................      u

    4-2   System of the use of waste  heat .......................      17

    4-3   District  heating  and cooling plant .......................      19

    4-4   The use rates of waste heat ............................     24



 5.  Power Generation  by  refuse  incinerator ......................     24

    5-1   Recent  situation of  power generation by
                refuse incinerator ..............................      24
   5-2  Operation .............................................     26



6 . Hot-farm  by  waste heat  energy ..............................     29
7. Road  boating.

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                                                                   262
8. Economy of  use  of  waste recovery heat	      34
9. Summary and studies of waste heat recovery	       37
                        END

-------
                                                                      263
 1.   Introduction








      Local government  are responsible for the municipal solid  waste disposal.




 But the collection of large quantity of conbustible solid waste needs many




 persons and machines.   Still only burning them in the incinerator  which is




 necessary to invest  lots of funds and technology in the construction is  ex-




 tremely unworthy.




      Since the Oil Crisis  in  1973,  as one of the global energy policy,  an




 importance of  an urgency of .saving-resources and energy  has  been intensely




 recognized.   As to solid waste disposal,  an  effective  use  of the resources  with




 keeping security of life-environment are  violently expected.




      The  method of  reclamation  of  solid  waste can be divided  into two ways.




 One is  reclamation of  energy, the other is reclamation of  material.  As regards




 of  reclamation, there are considered  in various methods.




      Next  three methods are  mainly considered.




 1) The  benefit  use of  solid waste heat.




 2) The  benefit  use of solid waste heat as a second fuel of burning coal.




 3) Refuse  is disposed by pyrolysis with the  state of oxygen shortage,  and




   reclamed to  second energy as gas, liquid oil etc.




   These above mentioned methods,  which experienced in Japan are for  the




 most  part  belonging to 1)  method .    Its heat is used considerably in   a  small




 scale, for examples,  social welfare facilities, a heated pool,  a home for the




old generation  and the power  to operate incineration  plant.  The positive  re-




clamation of  the waste heat is still  a  dawn of history.




      The city of  Sapporo has  been  positively  realizing  the waste heat reclama-




tion  of  municipal  refuse  incineration,  a  district  heating and cooling,  hot  far:r.




facilities,  power  generation, hot-pool,  road-heating etc.   It has been taken




notice of those  effective  savc-energy.   Operation experiences  are  ir.trcouced a =
                                      -1-

-------
                                                                 264
follows.
2.   Refuse disposal  abstract in Sapporo



  2-1   Topography and  countermeasure of  Sapporo



     This  city is situated in latitude 141°  21' east and 43° 01' north that is  in


the south-west of the 1 shikari  plain in Hokkaido,  and is  l6.9m above the  sea

                             2
and its total area is I,ll8km ,  the  circumference of city is 363  km, £2.3 kn


from east  to west and 45-4  km from south  to north.  It is  one of the  widest


cities  in Japan.


     From the topographical point of view,  mountains which are  located ir. the


part of south west ocupy three fourths of  city area.   The main  city fcr-ations


are developed as  alluvial fan that the Toyohira River runs through ir. the  ci:y,


and that the  Ishikari Low Land  is  spread  there.   The Tsukisamu  Terrace is ex-


panded  to  south east  of  the  city.


     Many  times  the  climate  is  under the influence of continent.  An averare


temperature however in  summer time is 20 "C, that  is easy  to  spend  generally.


The  winter begins in the early  November falling first snow.   High attr.cspheric


pressure from  Siberia grows and  brings  the cold and snow periodically.   Average


temperature in heavy cold time  in  January is ~5.5°C.   Once in a while  i:  is


chilly at about -20 tj.   The  snow  falls about 1 m deep at the  most and  its


accumulation  is  about 5  m deep at the  highest.   The citizen's  econc-.ic  activities


and lives are considerably  objected by  that snow  for  about  five mcr.th;  until


next April.  This city  was built in 1869  depending  upon an aim of ir.s  natictal


policy  to be  a  center city of Hokkaido.   Since then,  it is keeping or cevei":r|


as a center city in politics,  economy,  sccicty arc! culture 'iurir..;  a hu.-.Jr;: -i:u


ten-years of  birth.   The result was that  the population excorclod  a -.ill!"

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                                                                         265
 according to  the census  of  1970.


      The  total  population of this  city is 1,340,000  people in 1978, and  it is


 the  seventh city in population in Japan.  And the  industry classifications are


 0.2% for the  primary industry,  12.7%  for  the  secondary and 87.1% for  the


 third.


 It is one  of  the characteristics of that the industry inclines extremely  to the


 third industry.




  2-2  The collection and disposal of  waste refuse



      The collection of waste  had  been changed by citizen's  demand and  types


 of the collecting car after many changes of each house  collection,  refuse  box


 collection  of  a  few houses and its combination.   From  1972, collection areas


 have  been expanded throughout the city.  As the  most  useful refuse collecting


 system,  a station system has  been adopted.  An interval to  collect refuse is


 twice a week  as a city rule in considering not to  decomposit the garbage.


 And  then  from 1974, separate collection has  been  adopted twice  a week.


(Inco m bustibles, large-sized  refuse  are separated and  collected from the


combustible refuse)

                                                              2
      On regards transportation,  207  packer trucks  having  8 m   capacity  go


round and collect each area.  About  the  management and the  disposal of  refuse,


both the waste refuse  which the  city authorities directly collected  and industrial


waste  which dealers carried have  totaled to 740,000 tons in 1977-  There have


been  disposed at two incinerator plants  and three  landfill sites  as shown in


Table  1 in Sappcro.  The landfills are fully covered with soil by the  sandwiche,


system, and conveniently disinfected  by medicals.   As  to the sewage  at  the


landfill, the  sewage treatment plants  arc ma King effort  to prevent pollution.

-------
                                                                                                           266
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                                                                         2G7
2-3   The quantity and composition changes of refuse






      The national economy which was  rapidly developed from a period of i960




made great improve the national life and expand the productive activity.   On the




other hand, as the waste  "refuse" has increased in quantity  and  has changed




in quality and the refuse  disposal had turned to  a  serious  social problem.




The  changes  of  the waste  diposit and disposable  capacity of  Sapporo city are




indicated at Fig. 1.
            Fig.  1  Changes of refuse  collected and disposal
TOHxlO
       1973
                74   75  76  77  78  79  80  81   82   83  84

-------
                                                                      268
      The wates quantity is  514 g capita  day in  average in  I960,   After ten




years,  they  increased  in  about  1.8  times,  that is 910 g capita day, than com-




pared with in 1970,  as represented  Fig. 2  graphically that shows the transition




of the  waste.   Though the waste decreased partially, after -oil crisis at the  end




of 1973,  for the purpose  of  saving  resources, they have been  varied  to increase




again.




      The transition in  the cities of  Tokyo,  Osaka, Kyoto and Sapporo indicates




the radical  increase 2.5-3 times during  fifteen  years.




      The changing results in  Sapporo shows in  Fig.  3 that one person's refuse




discharged is 1554 g capita day 12.6  times  in 1977,  as  much as  that of 604 g




capita day in 1963.




      The waste to be accompanied with  the  income increasing and living condi-




tion  would be increased in the future.  The recovering  heat  after burning  up




the municipal refuse  waste is  utilized  effetively.  That means the refuse collected




is used as a fuel.   The quality and  quantity of the waste refuse,  especially the




heating value,  arc regarded to play  a part of great significance.   But  the
                        pin
               19*0 61 62  i! 44 « 66  67 1,3  69 70 71 72 73  71 75  '6 77  73

-------
                                                                  269
                          Tig 3  ch»ng«j of v«fuj« component in Sapporo.
                         1970   71   72   73  7">  75  76  77


                              __   I       I        	
                                                          1.600





                                                          1.600  ^

                                                               M
                                                               *
                                                               *".

                                                          l.WJO  t
                                                               u
                                                               jt



                                                          1,200  a

                                                               3



                                                          1,000  g





                                                        .' 800   |




                                                               §

                                                          600
           COLUCTUIO SfDTEM   IN CHARGE
                                   BO CHARGE  SEPARATE COLLSCTICN
important characteristics of waste refuse is a mixture of  every kind of all



things and  matters which is the solid waste produced by the  home life  and



industry.                                   s



      The volume and the component changes' according to  the  variation  of  the



seasons,  the weather,  and  the day of the week, so the waste refuse is not



actually constant fuel.



      From  the  point of view of component,  as  illustrated  in  Fig. 3, the



waste refuse more  than  45% of garbage and about  25% of paper  materials.



Recently the plastics in the waste  refuse  have been increased and included



around 10%.



As  there  are much garbages contained in  the waste,  therefore the humidity is



about 50%.   So  actually the combustible waste  volume is around  30°i.



      Compared  the waste refuse with the  natural fuel such as coal  and oil,



the  heating  valua of the  waste refuse is less than  that of the  natural  resources.



The low heating value  of the  waste refuse confined within  the  scope of  700-2000


kcal/kg.

-------
                  270
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-------
 3-  Refuse  Incinerator and  the use  of  waste heat.






   3-1  Continuous  municipal incinerator






      The  purpose of the  refuse incinerator is essentially  the  disinfection,




 the  stabilization and  the reduction of  the refuse.  Though the structure  of the




 incinerator is similar to  the coal  storker type of boiler,  the  refuse,  as above




 mentions,  involves  much humidity,  less  heating  value  than  the  coal.




      Moreover,  sucli refuse is so  unhomogeneous that the  incinerator is




 designed  taking a cope  with  it.




 Fig.  L, is  illustrated  the  section of one of the municipal continuous  incinerator.




      The  Refuse  that is grabed up by crane  from refuse pit,  is  reached on  the




 feeder  through shoot  from hopper,  and  is transported to stokers continuously,




 and  completely burned up after drying,  combustion and  embers.




      The temperature in the incinerator is maintained from 850 °C to 950X1.




 The  refuse is completely  burned  and the noxipus gas  is decomposed in high




 temperature.  The dust is collected  by  electrostatic precipitator and the other




 collectors  after dropping  the gas temperature 250-230*0.




      Waste heat  boiler is designed in order  to absorb the  heat available of  the




 gas  exhausted.   Thv steam generated is available to the heat  supplying  and  the




 generating electricity and so on.   As for boiler  type, watcrtube boiler  is




provided on  the incinerator which is  expected the radiant  heat  by waterwall.




     There is  provided two types of   boiler both which  are natural circulation




watertube boiler  and forced circulation  boiler.  Feed  water is open type.




The  steam  production is  1.0-3.0 tons per one tonnage of  refuse  bourncd, and




is  about 2.0 tons  in average.




     An available pressure and temperature of the boiler,  though  they are  required




to  use the  heat  produced  to the electric power generation, is  abci;: lo-^C kr,/c:n.




G  and  about  200-260*C  respectively.  But in Japan prc?r-i;:e  am! ;oi:;porriti;ro

-------
                                                             272
are properly designed to control below  25 kg/cm. G  and 280'C in order to




prevent high temperature corrosion  and  errosion of  HC1 and  SOx in the




conbustion gas.




     The  inlet  temperature  of  the gas to the electrostatic  precipitator is  also




maintained about 260 °C avoiding above 300 "C and  below l80°C in order to




prevent EP and  gas duct from  corrosion and errosion.




     Oil is used only  in  starting up.  The operation experience is  shown in




Table 2 at Atsubetsu incinerator plant in  Sapporo.
             Table  2    Operation Results at ATSUBETSU plant


YEAR
WASTE
INCINERATED
(TON)
DAYS OF OPER.
ASHES (TON)
METAL
COLLECTION
(TON)
IGNITION LOSS
(%)
DUST(g/NM3)
w
OT
3
t,
W
a:
o
fc3
o
12
0

-------
                                                               273
 3-2   The use  of waste  heat  from incin'erator  plant






      The  incinerators  have  proven to be modernized  in  successful- during




 these ten years in large municipalities.   Its  scale is concentrated around from




 450  T/day to 900 T/day.




      Almost all of these incinerators have prepared  the  waste heat boiler.




 The  waste heat is  utilized in the public  welfare  facilities,  such  as homes  for




 the old and hot pool, and is widely utilized as the power generation to operate




 the incinerator,  but  waste heat is not positively  utilized in  wide range.




      The possible  reasons should  be  probably as follows;




 1)  The  pressure and temperature of  the steam are restricted to prevent




     errosion of  the  boiler.




 2)  There  are  no large facilities  which waste heat is  available in  the neighbor-




     hood.




 3)  It may be  uncertain to have  the constant steam production for  the variation




    of quality  and  the quantity of  waste.   - "




 4)  The  use  of the waste  heat  is  varied  according to  the  seasons.




 5)  There  are  insufficient source of revenue  to construct the plant.




 6)  Even though there remains surplus electricity, the selling cost of electricity




    is restricted by  Electric  Utility Industry Law.




    The  cost of  construction  is  more expensive than that of the  common  steam




    power  station.




     As  for  the district heating to the housing, there needs the   waste refuse




of about  30-50 houses  to  get  the  heat  for one  house heating,  that is, the stcaTi




is produced 2.3 kg per  1  kg of waste, utilization of the  waste heat is  70?j of




2.3 kg, 633  kcal/kg  (IS atg,  240 °C) per 1 kg  of  steam,  considering the  refuse




collected is 700 g capita day  and four persons live in each house  commonly,




the heat  capacity utilized is coming from the 35 houses  prcsicciv; i:\ii  is




    633 x 2.3  x  0.7  x 0.7 x  £ x 35 x 1/2L =  LL^S  kcal/kg,  while in  case of
                                     -11-

-------
                                                                 274
                                                                   2

 apartment houses in one  place the heat, load of house is 80 kcal/m .h, the load


                                   2                                            2
 of hot  water supplied  is  10  kcal/m .h supposing the area  of each house is 50m ,



 the necessary heating  capacity  is  (80+10) x 50  = 4500 kcal/kg comprehensively.



      Therefore  it is impossible  that the recovery  heat  is  tr'ansfered to the all



 houses in the waste collecting area by only waste refuse.  The objective  district



 of servicing heat is largely different  from the waste collecting  district.



      Today,  the construction of incinerator is  objected  firmly by  the  inhabitants



 in neighborhood, so the administrations of the local  government  are required



 reexamination consequently.



      So  as  the  national policy,  it is  useful  that the incinerator is constructed



 by means  of  giving  benefit  to the  inhabitants  around the incinerator without



 problems.  That is the real meaning of  the  resources reclamation  and save-



 energy.




     City  authority  of  Sapporo  already decided that  model municipal incinerator



plants  should be constructed for  the purpose of the effective utilization of  the



waste heat at the five  places in  the city.   And  that from the point of view,



to improve the operation efficiency and to  prevent  the  pollution and to reuse



the energy in its district, a conprehensive plan is  prepared  to incinerate all of



the refuse collected.   To comply with  it,  two plants  have  already  operated and



the third  incinerator plant started  to construct in 197S in  Sapporo.



     The  experience of utilization  of the waste  heat  in the incinerator plants arc



prepared  in  the  table 3;  which  is distinctly  important in  the various  utilizations.
                                      -12-

-------
Table 3   Utilization of- Waste Recovery Heat.
PLANT
CONSTRUCTION
YEAR
START
END
Incinerator
Capacity
t/d
Waste
Incinerated
t/year
Recovery
Heat
Utilization Ratio
(of \
\/° 1
Plant inside

-------
                                                                      276
      Hassamu Plant  which has been operating from  1971  is  used to the  wel-




fare  facilities in the industrial factories.   Atsubetsu Plant  which  has been




operating from 1974 is used to the  district  heating  and cooling  in   the




urban district.   And the third  plant which is  now under construction will  be




used  in the hot farm development.




      At  the  same time, the power remained  after the independent electric




power will be sold,  and save-energy would be secured by the heat  supplying




system from  turbine  back steam after generating power.




      The ratio of the utilization steam of waste recovery  heat in Table  2  is




in Hassamu Plant of  the first construction utilized 53% of all the system generated,




and the release heat from  steam condenser,  namely  the non-utilization of steam




is remained 47%.   It should be improved in the future,  however.  Atsubetsu




Plant of  second construction has  77% of  utilization  ratio.   An  increasing




houses and buildings every  year in the district heating area  is expected to




increase the  utilization  ratio.




      The third plant is designed  to  use. to completed entire  utilization of the




waste  heat in many ways.   For the  above purpose extraction type of turbine is



adopted.
4.  District  Heating  using  the waste  recovering heat






  4-1  Abstract






     District heating and cooling in Sapporo is  operated in  six  districts




illustrating at Table  4.




     Equipment  capacity is reached 2S6 x 10 kcal/hour  using coal, kerosene




and heavy oil as fuel.



The  waste  refuse recovery heat  to the  district  heating  has beer; primarily

-------
                                                                                                                 277
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                                                                                                     278
                                                                              CD  1971-1974 HEAT SUPPLY
                                                                               ®  SUB-STATION
                                                                              -  PIPE LINE
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-------
                                                                       2"'9
 adopted for the first time at Atsubetsu £lant.




      The  servicing  district is  the east part of the city which is 12  km away




 from the center of the city.    The   district heating services Atsubetsu sub-




 center city  housing  development (31  ha), including  shops, the light industry




 housing development (273 ha) and Momijidai housing development  of about 7700




 houses.  Atsubetsu  Plant taking charge of waste recovering heat supply has




 two 300 t/D continuous incinerator is to dispose 600  ton refuse   at  a  day,  the




 steam generated by the waste heat boiler is  utilized to operate the  incinerator,




 and besides the surplus steam is positively utilized in many ways including  an




 district heating  and  cooling, an  independent electric power,  road heating,  hot




 pool,  green house.




      Fig.  6 is illustrated  heat  balance of  waste heat of Atsubetsu Plant.




 Fig. 5  is  shown district heating supply plan in Atsubetsu area.









   /r-2  System  of  the  use  of waste heat






      When 1 ton raw  refuses  (average low heating  value;  1600 kcal/kg) are




 burned  up,  2.3 ton of steam are generated.




      As illustrated in Fig.  7  as the heat utilization diagram,  5S t/h superheated




 steam  at 19  kg/cm.G,  240 °C arc  generated by  burning 25 t/h of refuse in  the




 waste  heai boiler.   Approximately  25% of those steam, in other word 25 t/h




 steam is used  for  the  machines  in  the  plant and 35% that is 20 t/h are  trans-




 ported to the back pressure turbine for the plant  electric power.




      After generation  of 1400 kwh power,  almost  all  of  the turbine  back steam




is served to a district heating  plant  at 1.5 kg/cm.G,  127 *C,  through low




pressure header unless 1.5% loss.




     About 23  t/h  high-pressure steam that is  £0%  of all steam,  is  directlv




transferee!  to a  district heating  pia/.t at 17  V:/cn  . G.  230 °C .  throu-ii  hi^h-




prcssurc header.   The  hot water  u; produced  in both  high and  low prj^s.ire

-------
Fig. 7   ATSUBETSU HEAT UTILIZATION DIAGRAM
                                                                280
    FROM
                                                             ^  &o'c-  I 'So'z
                                                              	

 CD  Boiler
 Q]  Super Heater
 Q]  Soot  Blow
 Q]  Steam Air Heater
 [5]  Boiler Feed Pamp
 E]  Deaerater
 Q]  High  Pres.  Steam Header
 IS  High  Pres.  Steam Condenser
 (2  Back  Pres.  Turbine
 OS  Low Pros.  Header
 IE  Low Pres. Steam Condenser
 D  Hot Tank
 1Q]  High  Pres.  Heat exchanger
 E)  Low Pres. Heat exchanger
 DC  Drain Tank
 OS  Drain Tank
 O  Deaerater Fer^d pump
High Pres. Steam

Lou Pres. Steam
Hot water or water
Control line
Control Valve
Pres. Indicator, control

Pres. Record, Control
Proportior.er

Pres. Control

-------
                                                                    281
 heat  exchangers (Parallel  flow) to be -utilized effectively for the district




 heating and cooling as one of the revivification to the peopel  who  live in the




 district.   These system  of both district  heating and  power generation to operate




 the  incineration  plant  are adopted.




      Yearly steam and  heat  balance are shown  in  Table 5 and  the  monthly




 variation  are illustrated graphically in  Fig.  10, respectively.




      In the  operation experience  in 1977, over all steam out-put was 440,000 ton




 of which  77%,  that is 340,000 ton of steam,  are utilized except  10  ton of  steam




 release in condenser.   In other word 144 x  10 kcal/ycar of  heat is utilized




 from  within 26l  x  10 Real per year.   As the result  an available heat efficiency




 is to be approximately 55%.    It  is  revaluated  to  14,400  KL in oil  in equiva-




 lent .




      Now  effective use  of  117  x 10 Real/year of heat (large in  summer time)




 released  from condenser should be  taken  into consideration









  4-3   District  heating  and cooling  plant






     The  energy plant  for district heating and cooling is co-provided  in  the




 same  plant in the incinerator plant, and  also  the stack  is constructed to




collect  together.




     The  designed  outline  of the district  heating and cooling  facilities are




as follows:	








Plant  out  put       :    77  G  kcal/h




Design  system      :   high temperature  Hot  Water Heating Pressure




                       10  kg/cm G




                       temperature   150 *C/SO *C




Pressurizing System:   constant  N   GAS  pressure
                                   -19-

-------
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-------
                                                                           283
 controling




 Zone  controling




 commection system




    of primary  and




         secondary




 cooling  system




 pipings








 piping extension








 flow speed




 pipe diameter
flow control




block substation  system
Breedin  system




high temperature absorption rcfrLgerater




primary-steel  pipe conduit




secondary-NI SHI GATE  flexible  pipe




primary-14-  km




sccondary-37  km




1  m/sec   (standard)




primary - 50-350 mm




secondary -  50-200 mm
       Though it  is possible that  more than 60%  of  steam generated is utilized




to the district heating.    V/hen the load required is comparatively  low, the




steam  remained is  released in the cooling condenser.    On the contrary when




in shortage of heat,  satisfied heat is preliminary supplied by the four boilers




at district heating  energy plant (6/+ Gkal/h).




       From December in 1974 utilization of waste heat is  initiated to serve at




the 2,500 municipal houses, since then it  has  been increased every year, and




now  served to 6,300 houses.




       The experience in 1977 shows  that heat demand  of the district heating




was  about 67  x  10  kcal  while  the waste  recovery heat  was  used  57 x 10 kcal




which  means S5% of the utilizing  ratio .of the waste heat and that  about 5,700 KL




of oil  were  saved  in a  year  in equivalent.




       The utilizing ratio of the waste heat is  desired  to maintain above 60s.-




when  the  houses  development  would be completed  in l°S-~.
                                      -22-

-------
                                                           284
                   •b^oBMhv^^L—JZ.^^ - _
Fig. 8 Atsubetsu .Plant  (Lower) and district heating
       territory  (Upper)
                     (photograph 1)
                              2
                             4?
                                                                    ~
                                            -v 5. <»

-------
                                                                                                                                285
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-------
                                                                        286
       The  result and the hypothesis  are shown  in  Table 6.    Table 6 explains




of the future of heat utilization.








   4-4  The  use rates of  waste heat






       The  supplying rates of waste from the incinerator plant  are decided



Y 0.65 per  1,000  Kcal  (Y 3.5 for the  1 ton  of  the  steam) from the cost




accounting of the steam  equipment  in the incinerator plant, after  taking into



consideration of those of  the demand  of the inhabitants near the plant,  the revivi-



fication to the district and th'e expensive pre-investment in the  municipal  houses



and district  heating facilities in  long terms.



       The heating  rate  system of the district heating enterprise is thai for



the apartment house  fixed amount system is accepted for the independent  houses



meteric system  accepted.    An annual heating rate  is  about 64,000 yen for the



2DK,and  about  73,000 yen for the 3DK.



       Compared with the  heating rate  at Makomanai  district without the utiliza-



tion of the  waste heat,  the  rate  utilized the  waste  heat  is cheaper 15,000 yen  in



a year than  un-utilized.



       This  explains  that cost is  returned to  the district  people.
5.  Power Generation  by  refuse  incinerator






  5-1   Recent situation of power generation by refuse incinerator






      Most of  power generations  at refuse incinerator  in  Japan  arc small one




which spend   only in its incinerator plant.   The  main reasons arc  as follows;




1)  By  Electric Power Supplying Law,  the  power  service is monopolized




    according  to territories by only 9  electric  supply companies  so  that no
                                    -24-

-------
                                                                 287
      one can  deal with it  except  them.- In addition  sales cost is restrained




      extraordinary cheap, on the contrary purchase  cost  is expensive several




      times as above.




 2)    The  parallel electricity are available,  one  of which  a security  preserva-




      tion  electricity coming  from electric  company have been  under an obligation




       in basic payment even if  without  supply in normal operation.




 3)     Being caused by large flucuations of generated power in  incineration




       plant in proportion as refuse callories  as  well as its attending  volume,




       the  electric power company has  some difficulty in controlling services.




 4)     The construction of municipal incinerator power plant  recovering whole




       refuse  energy from  incinerator charges too much  to the  local govern-




       ment .






       Recently,  however the attendance of high-calorie refuse  has been




 making it  possible to generate more  than  power than  that  to operate the




 incinerator.    And for the benefit of the resource recovery the electric




 company has been assumed a position of  purchase of  the refuse-generated




 power production,  from the municipal incinerator plant.    There have  been




 many cities who  have incinerator  plant  in  Janpan  to  rcclamate  overall  refuse




 waste  heat.    The city of  Sapporo has  undertaken the construction of the




 Third  incinerator power plant in 1978.




       The power generation  until  now had  been limited  to  generate to




operate the incinerator.    That  is approximately  50-100 kwh from one tonagc




 refuse.   Meanwhile  overall  waste heat  reclamation to  the power  would




considered in potentiality to  have  a capacity of 400 Kwh from one  tonagc




refuse, while for the  prevention of high and  low  temperature corrosion and




an account of a large amount of  steam  comsumption in incinerator  piant,




power production  is actually  estimated about 250  Xvh one  tonr.ge refuse ever,




if  employing condensing turbine.

-------
                                                                     288
       Actual  incinerator plants in Japan are  basically applied next forms  of




 type  as shown in Fig. 10.




       Type  a :   Steam  Operates  incinerator and surplus steam  is cooled by




                  air condenser.




       Type  b :   Power generation by  steam  turbine  operates the incinerator, and




                  turbine  back  steam  is cooled by low  pressure air condenser.




                  surplus steam is cooled  by  high pressure air  condenser.




       Type  c :   Power generation, district  heating and other heat  exchangers




                  are applied in parallel.   Turbine back steam  is cooled by




                  low pressure air condenser.




       Type  d :   Power generation, district  heating and other heat  exchangers




                  are applied in series.   Turbine  back steam is reused to




                  the  district heating  and other heat exchangers.








  5-2   Operation.






       The city of Sapporo in its  high latitudes of territorial aspect has been




making  a  best effort to recover refuse energy.   One of those is Atsubetsu




Plant that  has  1,400 Kwh power generation employing back pressure turbine




and has supplied  waste heat to  the district heating.    And  another is the  Third




(Fukui) Plant  that has 4,800  Kwh  power generation  employing back extraction




turbine and has heat exchangers for the hot-farm.    Both plants  adopted d type




that  is  conbined with power generation and turbine back steam to the farm.




       Operation result as shown in Table  7,  at  Atsubetsu  Plant  in 1977 over-




all power generation out  put is 3.695 MV.'H in a year  and its rate of  operation




is 94?a.    The power  depending on plant generation  is  rated 95""; in  average.




More  than  99-J pcver  depending rate  on  plant  generation is  experienced for 7




months  and  saving in charge of electricity (the charge of  payment to commercial




power)  was ¥75,000.000  in a year.   And also the  Third Plor.t  is possibly
                                -26-

-------
                                                              289
Fig. 11   4 BASIC TYPES OF POWER GENERATION
                    PRESSURE-ENTHALPY DIAGRAM

-------
                                                     290
Table 7   Power Generation of Ataubetsu Plant
ANNUAL
GEN. POWER OUT PUT
(KWH)
PURCHASE POWER
(KWH)
OVER-ALL POWER
(KWH)
GEN . POWER i!?/HL
™"« ™usf
PUKCHASE <™|OB
P01"E« REFUSE
GEN. OPER. RATE
(01 \
(i°l
RATE DEPEND ON
PLANT GEN. (%)
GEN. COST
(Y x 1000)
PURCHASE COST
(Y x 1000)
REVERSE POWER
(KWH)
REVERSE INCOME
(Y x 1000)
1975
MONTHLY
7,028,700
1,631,200
8,650,900
-
-
-
-
51,684
29,002
-
-
YEARLY
637,427
124,045
761,472
41.22
8.44
83.3
83.3
4,687
2,339
-
-
1976
MONTHLY
8,379,700
508,700
8,888,400
-
-
-
-
69,591
20,078
-
-
YEARLY
745,554
33,154
778,708
45.48
2.4
93.5
95.1
6,179
1,584
-
-
1977
MONTHLY
8,694,600
446,680
9,141,280
-
-
-
-
75,116
21,018
514,400
1 , 543
YEARLY
781,536
27,880
809,416
46.28
2.0
94.1
95.8
6,747
1,671
171,467
514

-------
                                                                    .£91
 estimated  to economize ¥230,000,000 in  a year that  in corresponded to 35,000



 MWH.



      Concerning  surplus  electric power,  under the condition which is not applied



 the  Electric  Utility  Law, Atsubetsu  Plant has  transmited its surplus  power of



 1,500  Mwh to  outside in a year  that is  corresponded  to ¥4,500,000 incomings.



 Likewise The Third Plant  is estimated to transmit  its surplus power to outside



 13,000 Mwh in a  year,  corresponding to ¥40,000,000 incomings.
6.   Hot-farm by waste heat Energy





      •The Third  Plant is now  under construction  at  the agricultural promotion



territory,  15 km northeast from city.   With desire  of  the community  people,



hot-farm is planned to develop making a  full use of  the waste  heat energy,



that is  expected  to  flourish self-supply  of  the  fresh  and green  vegetable  to



the city during the  snow-full winter  time to keep security  of  agricultural economy,



cutting    the indispensable heating expenses.



      This  site of the hot-farm had been  completed by landfill by solid waste



disposal.  The foundation was  an  alluvium  of lower  moist  ground to be con-



situted  by  the meandering stream of  the  I shikari River.



      The peat  bed is  lain 4 m directly be'ow  the earth surface,  and  as  far



as  approximately 20 m downward a weak  accumlation  stratum, including silt,



clay, sand,  saprolite  are taken occupied.  The refuse  was spreadeu  and  con -



pactcd by bulldozer about 5-6 m in thickness and covered  with  scil 1.5 m in



thickness which had been obtained immediately  in front  of  the face there.
This is better to  pay  attention in  the  point of view of reuse of lar..'.fill site.



     Hot-farm consist of 60 hot-houses  being  500  in in each will  be  supplied


                                       2
23-5 ton per  hour of  steam  (at 5 k£/cm"G. l~j>.S C) which ..:•!  ...oan 1.1 Gcal

-------
Fig. 11    HEAT BALANCE OF THIRD PALNT
1987
22.44
3.84
0.39
8.83
3.18
 LOW PRESSURE  STEAM COHDEHSER
	PRAIN
                                        POWER GENERATION
                                        —-I.
4.59

1.19
            DRAIN
            0.07
          HOT-FARM
             2.77   ROAD HEATING
                                             20.5'
                                             25.21
             DRAIN
                0-.51  HOT-WATER
             (DRAIN
               0.05
          NO.l GAS REHEAT
      DRAIN	
       2.47
       AIR CONDITIONING
                                4.35

                                0.44
                                                  53
                                                   TO  PREVENT CLINKER
                                                         ;1.02
                                      11.30
               0.43
                    DEAERATOR
                                   3.61
                7.63
                 No.2 GAS
                     PF'jF A'l'
        DRAIN HIGH
        1.90
                DRAIN
                0.04AIR HEATER
                RETURN DRAIN
  7.63
JUREINE,_SUPP_L '/_;.
      79.66

D .49
E STEAM CONDENSER
BOILER ABSORPTION
                               10.5 (     "1.4

                               0    !
                                                    Slow
                                                  0.52
                                              EXHAUST  GAS
                                                           25.10
                          -30-

-------
 per hour.  The steam shall  be  converted to 40 °C hot water  through  heat


 exchangers at hot farm to force cucumberes, to raise tomatoes and to grow


 green vegetables,  cultivating 3  times  in  a  year.


      Hot farm  management shall be administrated  by a  cooperation anticipating


 farmers under  the leadership of agricultural center of City  Authorities in


 neighbourhood.    District heating technology using waste recovery heat should


 practically  be available in this  hot  farm.   Fig. 11  explains heat balance of


 The Third incinerator plant,  and a photograph of  the plant and hot farm  is


 presented in  Fig.  12.


      Facilities  of  hot-farm is as follows :	


 1)  site area :      10 ha

                                      2
 2)-  facilities :   60 hot houses  (500 m each)

                                          2
                  6 seedbed  houses (500  M  each)


         additional facilities   :   management building


                                 equipment  building


                                 ware houses


                                 parking   site


3)  Houses   :           vinyla house construction


4)  heat exchangers :


    for the  cultivation  supplying  80 "C    returning  60 °C


    for the  seeding    supplying  40 "C    returning  20 °C


5)  auxiliary  boiler    three 2.2 Gcal/h  boilers


6)  management         coorperative organization
                                    -31-

-------
                                                                  294
                                                     Fig. 12
                                                      Third Plant and
                                                      hot-farni
                                                           (photograph  2)
7-   Road heating

     2.5mm steel  pipes or  nylon  pipes in diameter pitching  100 - 160 mm are
layed,  under main  inlet  and  outlet road and  ash disposal  place in the incinerator
plant site.  70 "C  hot-water  including ethyleneglycol via heat exchanger after
steam turbine are continuously  circurated  by pu.'.ips to be melt snow  in
winter.   The temperature is  controlled automatically.
                                         2                          2
     Road heating  covers  area of 2600 m  at  Hassamu  Plant,  590C m  at
                            2
Atsubetsu plant and  11000 m  at the Third  Plant.  Snow melting heat  required
is designed 370 kcal/m.h  under the  condition of  40 mm  snow  per hour, -9 *C
snow temperature and 80-85% heat efficiency.    Practically  experienced data
                        2
mentions  180-200  kcal/m^h heat  consumption in average.
     The way of execution,  as  shown in  Fig.  13, is  that 25 mm styrcl-foam
in thickness (foaming polystyrol  plate) is  covered on the roadbed on  which
25 mm  steelpipc or  15 mm nylor.pipe  is  set within  the center of  2CO mm
concrete in  thickness.
The  road surface  is  covered with  40 mni  asnhalt  in thickness.

-------
                                           295



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                                                       63



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-  33  -

-------
 5.   Economy  of  use  of  waste recovery heat
      The ultimate  responsibility for the collection and disposal of municipal

 refuse rests with local  government.  So  economy of  use  of waste recovery

 heat  should be discussed.    It is quite difficult in equipment to make distinct-

 ion between refuse incineration and utilization of waste recovery heat.

 However, boiler, steam turbine,  power generator,  steam  condenser and  those

 fittings are considered to the waste heat  recovery facilities.    The cost of

 those waste heat recovery  facilities are  assumed about 20% of  all cost of  the

 incineration plant.

      Both Atsubetsu  Plant  and The Third Plant  are  600 t/d in capacity to

 incinerate.    The formers  cost of  heat  recovery facilities is  Yo79,700,000

 in 1972, while the  other's  is  Yl ,324,000,000 in 1978.

      The incomings on the  one hand contains power  saving cost (an equivalent

cost when paying to the commercial  power),  sale cost of  reverse power

(Y 3  for 1 kw)and  on  the other hand outgoings contains operation  and

maintenance cost of the heat recovery facilities including  5%  anr.ual increas-

ing cost, and  also  contains  personal cost which  is based  on  4 person's wages

of Y3,550,000  in 1975 including annual 6%increasing.  Using  above as a basis
                                                      Fig.  14

                                                       Setting  of  r^ad  heating

                                                       pipe
                                                           (photograph 3)

-------
                                                                                                                      297
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-------
                                                              298
 Atsubetsu plant is neccssiated  to amortize in 8.5 years and  The Third

 Plant in 7.5 years,   An  graphically explanation is  shown  in Fig. 15.
           Fig    Amortizing yenrs for the utilization
                   facilities of  the waste heat
 20.-
                                                                     15
      NOTE:-  Outgoings  include  construction  cost
     An effect of economy of utilization of  waste heat recovery as  shown in

Table 8 evaluates the depreciation amount ir.ihrcchy  at compound interest

carrying 6*i  interest in a  year  for 15 years depending  upon the lc<;al life of

Japanese Ministry of Finance, nanoly:
                                  -JO-

-------
                                                                         299
              AQ+0.06) - 0.06A




                  (1+0.06) - 1






       A is the  cost  of  waste heat recovery facilities.




       When including the cost increasing power and steam and  government




 financial supporting fund  for the facilities,  this  economical effect  is  clearly




 apparent  to increase.




       If  not combined with  heat recovery boiler,  cost of  construction is




 comparatively low.   And there are no merits of  income  and revivification, to




 the district.
 9.  Summary and studies  of  waste heat recovery







      Operation experiences  give  next considering problems.




      1)  It is difficult to control the  disposing  quantity of refuse according




 to the  fluctuation of  waste recovery heat-demand.    An  effort of keeping




 counterbalance by controlling heat demand and a development of  technology




 for a huge  amount of heat accumlation  should be desired.




      2)  It is certainly beneficial to generate power by  extraction  back turbine ar.d




to  use the waste heat to  the other  facilities following up the heat load fluctuation,




 and to  reverse the surplus power to outside.    So  positive heat deranci in




 summer time should be investigated.




      3)  Under the circumstances of technology  of  today  steam  condenser as




 though  quite  expensive  is necessary  result.




      4)  Following up characteristics of  controling to keep balance  of  supply




 has time lag ond  is not reliable.




      5)  As  safety range  of  high and  low temperature corrosion. i.c  :: -i:o-i




 quite in narrow,  design requirements of boiler a::U turbine (ste.v..  • c. -porn!1..re.

-------
 Fig.  16    AVAILABLE SYSTEMS OF  POV/ER GENERATION




                BY WASTE RECOVERY ENERGY
                                                                    300

V
§"
t£ U
w: -.:
V  w.'tIf
-------
                                                                 301
 types,  output, how  to operate) should -be taken into serious considerations.




      6)  Incinerator plant in Japan has to stop to operate about  20 days once



 in a  year for the regular maintenance.   Auxiliary boiler  should consequently



 be  equipped for the waste recovery heat user.








      In conclusion,  as  one of the  future case studies  of  waste heat recovery,  it



 is a  suggestive  information  that The  Scientific Technology  Researches of



 Resources has investigated power generation systems from the  waste recovery



 energy  and that the results  of the  study have been published as  shown in Fig.



 16.




      Electric powerproduction  from refuse  is  generated only for  incinerator



 plant,'but for the further effective  study the combination with commercial



 power plant and  refuse  pyrolysis should be considered  in  for the multi-purpose



 utilization of  waste  heat.



      In  Japan nowadays  the  constructionslof incinerator plant face to



 difficulties in which the  area people are against  them.    It is commonly



 speaking  that  obtaining of better understanding and strong cooperation of  the



 area  people complete almost  of all construction.



      Beneficial use of large amount of  waste recovery heat and  its revivifi-



cation to  the  area people  would inevitably be connected  to the area people's



understandings and cooperations.



      Refuse reclamation of  saving energy would  steadily be made progress.
                                   -39-

-------
                                                                           302
              An Effective Use of Waste h'ca~L of Refuse Incineration
                    — The Experience in Sapporo City
                 Discussion Leader:  Dr. Hiroto Mitani
Question:  What kinds of plastics make up the 10 percent fraction of

           plastic in the waste stream?

Answer:    We have conducted some research on the make-up of plastics

           in waste,  but we just don't have those figures with us today.

           However, we have not done any research on quality—quality

           of plastics in waste.  Figure #J in my paper gives you an

           idea of the make-up of the collected waste.  And at this

           point, we can say that plastics collected in the form of

           bottle containers account for the rr&jority of the plastic

           waste.  Quality-wise, the plastic waste is composed of

           polythylene,  polyester  polyvinylchloride and synthetic

           rubber.  The major of the plastic will be polyethylene.  As

           Mr. Miyanohara from Yokohama, City told you yesterday,  poly-

           vinylchloride seemingly poses major difficulties for treat-

           ment, but at this point it is still an issue that we mast

           explore.  However,  from the production side, we have come

           up with some estimated figures.   Ten percent of all wastes is

           plastics.   Of that 10% plastic waste, 70% is polyvinylchloride.

           That makes polyvinylchloride 1.7% of all our accumulated

           total waste.

Question;  Was your original goal for building a refuse incinerator volume

           reduction or energy production?

Answer:    Since safety,  stability and reduction of solid waste are

           major issues in Japan, volume reduction was more important

           than energy production.  Heat recovery from incinerators is

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                                                              303
           very  important from the viewpoint of resource recovery,but




           in  most cases the public resistance in Japan is very




           strong against facility installations.  So we try to make




           heat  recovery beneficial to the community.  I can say that




           the case in Sapporo is a successful one.




Question:  Would having a higher energy utilization ratio make the




           plants more economically viable?



Answer:    I can see the point that you are making—having higher energy




           utilization rates will make the plants more economically viable.




           However, as I just mentioned,  it is dangerous for us to favor




           energy production over refuse reduction.  I pointed out some




           reasons why some of us are not taking a very aggressive approach




           to heat recovery from incinerators.  Energy utilisation is




           very  important; however, it is also very important for us to




           consider local needs.




Question:  What are the primary goals of other Japanese cities?



Answer:    I think that primary goals of most Japanese cities would be




           sanitary treatment and reduction of waste.  As I mentioned




           before,  we have a very short history of heat recovery and




           we just started utilisation of heat recovery from incinerators.




           I don't have the documented figures with me, but as I recall,




           in Japan,  there are approximately 360 continuous operating




           incinerators.   Of those 360 incinerators,  QQ are those with




           boilers which makes them feasible to use heat recovery.   Of




           those 360,  26 facilities have  electric generation equipment,

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                                                         304
but those are pretty small scale; these 26 are mostly used




for their own operation.   Those facilities that utilise




electricity for sale are limited to some cities such as




Tokyo, Sapporo and Osaka.  As Chairman Morishita pointed




out yesterday, quite a few cities in Japan are now con-




sidering heat recovery from incinerators because of the




fact that volumes  of waste are increasing.

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                                                   305
4.   Resources Recovery Technologies
            4.3  Composting System :  Part 1
                            by
             Sachiho  Naito,  Dr.  of Engineering
    President,  Sachiho Naito Consulting  Engineers  Inc.
    Lecturer  of Musashi  Institute of Technology

-------
                                                           3C6
                               Contents


                                                                 Page
1.  Introduction
2.  Investigation of Domestic Waste 	   1

    2.1  General 	   1

    2.2  Result of the investigation 	   2


3.  Evaluation and Improvement of Existing Composting System ...   6

    3.1  General	   0

    3.2  Economical evaluation of existing composting plants ...   6
4.  Research on Evaluation and Improvement of the
    Composting System 	
    4.1  General	   8

    4.2  Conceptional design for composting system 	  10

         4.2.1  Condition for the design 	  10

         4.2.2  Input conditions	  10

         4.2.3  Output conditions 	  10

         4.2.4  Result of conceptional design 	  11


5.  The Design of Separate System for Hazardous Material 	  14

    5.1  General 	  14

    5.2  Content of hazardous materials in raw refuse 	  14

    5.3  Effect of the separate collection 	  15
                                 - i -

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                                                   3O7
                                                             Page

5.4  Investigation on the effect of separation
     techniques	   17

     5.4.1  Objection 	   17

     5.4.2  Contaminants and composting system 	   17

     5.4.3  Operation of separation 	   17
                           -  ii -

-------
                                                         3OS
                  Part 1:  MODERN COMPOSTING SYSTEM
                           By Dr. Sachiho Naito
                              President,
                              Sachiho Naito Consulting Engineers Inc.
                              Lecturer of Musashi Institute of Technology
1.  Introduction
    It is a common problem in the world that composted material made
    from domestic waste has not much market.  Especially, demand of
    composted material is limited and the materials are accumulated in
    the country where inorganic fertilizer are utilized heavily.  The
    longer the transportation distance, the more the cost is and there-
    fore a demand for the high cost composted material is very limited.
    This has been the story for recent years, but the other type of
    story came about in last year or so.   That is the heavy metals in
    the composted materials which are not favour for the soil.  In Japan,
    Ministry of Agriculture has set the temporary standard for the allow-
    able heavy metal quantity in the composted material.  That is 2 ppm
    for mercury, 5 ppm for cadmium, 50 ppm for arsenic.  The question is
    whether composted materials made from domestic waste contain more
    than allowable quantity of those heavy metals.  It is necessary to
    clear this doubt before making any decision on financial aid to the
    municipalities where the composting systems are scheduled to be
    built.  In order to discuss this particular problem, "The research
    on the improvement of composting system and the agriculture usage
    of domestic waste", which was conducted under the directions of the
    Ministry of Health and Welfare, is reported as follows.

2.  Investigation of Domestic Waste
    2.1  General
         Generally speaking, the composting system is suitable for
         relatively small towns which may be categorized as an agricultural
                                 - 1 -

-------
                                                 309
     town rather than an urban town, because the market for com-
     posting materials is very important and an agricultural town
     can expect good market.  In this study, the towns under 50,000
     population are categorized as urban town, agriculture town, or
     intermediate town.  The domestic wastes which could be resource
     material for composting plants were investigated.

2.2  Results of the investigation
     For the pure urban town, the paper content is relatively large
     and the content of garbage is relatively small.   Wastes in
     agricultural town is in inverse, and domestic waste in highly
     urban town contains more water than agriculture  town.  In
     general, the garbage content ratio in total waste in winter
     time is more than that of in summer time.  They  used to say
     that the garbage in summer time is more than that in winter
     time, but I would say this statement is not necessarily true.
     Result is shown in Figure 2.1.  In Japan, there  are some
     differences in paper and garbage contents between western
     part of Japan plus pacific ocean side and other  area, big urban
     cities and small towns, and pure urban towns and agricultural
     towns.  The formers contain more paper and less  garbage than
     the latters.
     Figure 2.2 shows C/N in composted material in these three
     different types of cities.  In any case,  C/N in  autumn is
     lower than that of in summer and winter seasons.   There are not
     much differences in C/N among pure urban  town and intermediate
     town except summer season, but C/N of agriculture town is lower
     than those.  There is some relationship between  C/N and the
     quality of domestic waste.  Usually,  we can say  raw agriculture
     waste contains  less paper and more garbage than  that of pure
     urban town and  intermediate town.   It is  concluded that C/N
                            -  2  -

-------
                                                 310
depends on the quantity of paper in domestic waste.  The waste
generation per capita per day is quite different from city to
city and there is no similarity in quantity.  In general, the
waste generations per capita per day in those investigated
cities are relatively small compared to the national average and
this may be explained by the size of the cities investigated.
The seasonal variation of refuse quantity is as follows.  The
local maxima lie in August, December, and March, and local
minima lie in February and November, and maximum quantity is
found in February.
                       -  3 -

-------
                                                           311
 Summer
Autumn
Winter
I— Paper



   Garbage



   Plastics



— Water



— Paper



   Garbage



   Plastics



 -Water



— Paper



  Garbage


  Plastics



'—Water
                                             Dry basis:  Weight (%)


                               0   10   20   30   40    50    60
                                        JL
                               ///////////77/A
                              '///////////////////T
                               '/////7////A
                                  '
                               '///////////////A
                                            Urban town




                                            Agricultural  town




                                            Intermediate  town
  Fig.  2.1  Seasonal Variation  of  Physical Composition

            in Domestic Waste

-------
                                                  312
                                C/N
                    10       20      3,0      4,0      50



City I

Agricultural town

City H


Intermediate town
City K








''^/'^/^/^//^^^^^^^/
',•'.'.•': •.'•'.'•'.'• ••"•':'•'.'.••.' '••••.' '.-.'. .


W//W////////A



7^^^/^^^/^^/'/


Summer

Autumn %%%%%'

Winter •'•''. .'.';•;


%








• - •• -1






Fig. 2.2  C/N in Composted  Materials
                  - 5 -

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                                                            313
Evaluation and Improvement of Existing Composting System
3.1  General
     In order to evaluate the composting system financially,  the
     existing operational composting facilities were investigated
     and the costs are compared with other types of disposal.

3.2  Economical evaluation of existing composting plants
     There are the cities T,  H, S and H,  where the composting
     plants has been under operations.   It is  difficult  to  expect
     the same results among those cities  because they have  their
     own different local conditions.  However, the ratio of the
     labour cost in total cost is relatively large in either cities
     and it is true for the city where the depreciation  cost is  not
     included in the management cost.   Here it is assumed that non-
     combustible waste,  bulky waste, and  direct carried-in  waste are
     disposed by landfill and only combustible waste may have
     different alternative disposals;  incineration,  composting or
     landfill.  It can be said that total cost of landfill  is less
     than other 2 systems,  but incineration and composting  are al-
     most same.  If the  sales income from composted  material is
     taken into account,  the  composting system has a little more
     advantage than incineration.   The  key factors of this  comparison
     are cost of transportation and landfill disposal of residue.
     Incineration generates about  10 to 15 percent ash (wet basis)
     of  raw refuse.   Composting system generates  residue about 50
     percent of input refuse.   Therefore,  it is  hard to  believe
     that composting system is  better  than incineration.  As a
     typical example of  this  investigation, composting system is
     shown in Figure 3.1  for  the  city T in 1976.
                            - 6 -

-------
                                                                                                               314
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                                                 -   7  -

-------
                                                         315
Research on Evaluation and Improvement of the Composting System
4.1  General
     Several private companies were asked to make conceptional
     designs with 50 tons per day disposal capacity to develop the
     composting system for domestic waste.  There are much differ-
     ence in developing efforts among the private companies.  Some
     companies are so enthusiastic to develop the composting tech-
     nology and,  some are not.  In any case, they intend to develop
     the composting system to produce the high quality and loss
     contaminate  composted material with considerations of the
     experience obtained during 1955 through 1970 when the compost-
     ing boom was declined.   For that reason,  improvement of the
     composting technology contracted with foreign countries are
     made in addition to the improvement of the post-digestion
     facility. Table 4.1 shows the existing composting systems
     under development.   In  this table,  there  are 8 private companies
     and their partner companies in foreign countries,  the type of
     digestion tank,  historical background of  technology develop-
     ment,  and characteristics of the systems  are tabulated.
     From this investigation,  it is known there are two major con-
     ceptions  for the digestion process.   The  first one is as
     follows.   The  main  part of this  system is  the digestion tank.
     The concept  is to produce the  high  quality composting material
     within relatively short period (3  to 14 days)  utilizing
     effectively  the  digestion mechanism.   The  other one is as
     follows.   First  of  all,  the quality  of  solid waste is controlled
     and particle size is  unified.  Then,  the waste is  transferred
     to  the  fixed silo or  storage area and digested during relatively
     long period  (20  to  30 days) .   For shredding  and separation,
     there  are  two  major  types.
                            - 8 -

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                                               316
Table 4.1  State of Art of the Composting System
Developper
Ebara-
Infilco
Takuma
Nihon-
Seikosho
Tsukishima
Kikai
Fuj i-Car
Fuji
Electric
Mitsubishi
Heavy Ind.
Yasukawa
Electric
Technology
Contact
USA
(Nov., 1976)
Italy
(Feb., 1977)

Switzerland
(Dec., 1975)




Digestion Tank
Circular, Fixed
Type
Rotating Drum,
Indoor Type
Bin Type
Windrow
Multi-stage,
Fixed. Type
Earp Thomas
Rotary kiln &
Silo Type
Circular, Fixed
Type
History of Development
Test plant, 1 t/d at
Koyama Tochigi Pref.
(Mar., 1977)
Pilot Plant, 10 t/hr at
Takasago, Hyogo Pref.
(Oct., 1977)
Basic experiments since
1973, 3/hr; Conducting
Research under contract
with MIT I.
Since Jul. , 1976, shred-
ding and windrow compost-
ing has been tested.
Test plant at Osaka, 1/d;
110 t/d plant at Saga City
since 1975.
Plant study of 1 t/d at
Yokosuka research center,
Dec., 1976 - Mar., 1977.
Pilot plant of 1 t/d at
Hiroshima, since Jun. ,
1977.
Experimental works with
a series of system at
Fukuoka.
                     - 9 -

-------
                                                        317
     The first one is the type which applies grinder in the front-
     end and utilize a combination of various separation devices
     depending on materials to be removed.  The other type is the
     system which uses rough shredding in the front-end to remove
     glasses, metals and plastics.  To remove plastics and others,
     many separation methods; magnetic device, air classification,
     and bouncing separation, can be applied.

4.2  Conceptional design for composting system
4.2.1  Condition for the design:
       The followings are conditions assumed for design,
       Capacity:       50 tons per day
       Specification:  shall be based on the guideline on a standard
                       specification concerning the construction
                       project for solid waste management which were
                       prepared by Japan Waste Management Association.

4.2.2  Input conditions:
       Solid waste material to be composted is wastes which is
       collected by source separation namely non-combustible waste
       and bulky waste.   This combustible waste is disposed by a
       composting plant.   Physical compositions of assumed waste
       are given on dry  basis and wet basis.

4.2.3  Output conditions:
       Plastic materials  are cut down in less than 2mm size.
       Metals are removed as much as possible using magnetic  devices.
       Glasses are desired not to be included in final products.
       Odor:  No bad smell from final product.   It is favour  to use
              aerobic digestion if it's possible.
                            - 10 -

-------
                                                              318
       Degree of the decomposition:  To be decomposed as completely
                      as possible.
       COD:           Don't contain COD element which causes
                      secondary pollution.
       Heavy metals:  Don't exceed the temporary standard
                      concerning hazardous component in the special
                      fertilizer.

4.2.4  Result of conceptional design:
       The conceptional designs were submitted by 8 cooperative
       private companies.   Designs are conceptional and it is not
       sure that the design conditions are all satisfied.   Because
       some companies are  not operating any composting plants and
       some of them have developed or  in developing stage.  Design
       conditions are not  clearly understood.   Those are understood
       differently by company to company.   Some companies have
       spent a lots of efforts to simplify the system and others
       employ several stages of separation processes.   There are  big
       differences between upper and lower limit.   The costs of
       construction and operation are  not  compared on the same
       basis.
       Generally speaking,  it can be concluded that the cost for
       composting system is not cheaper than incineration or other
       disposal method.  For the design of 50  tons per day capacity
       facility,  the average cost of 6 companies excluding the high-
       est and the lowest  is 574 Million yens.   (11.5 million yens
       for each ton of raw refuse).  These costs  are about the
       same as the incineration plant  and  operating cost may be the
       same.   If the disposal cost  of  residue  is taken into account,
       the cost for composting system  is much  more than other dis-
       posal  systems.   Over all,  it  is impossible  to compare the
                            - 11 -

-------
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-------
                                                                 320
         Table 5.2  Content of Heavy Metals in Colored Paper
                                                               (PPM)

Hg
Cd
As
Green
L
0.01
ND
12.95
D
ND
ND
1.05
Blue
L
ND
ND
9.92
D
0.02
ND
0.94
Red
L
ND
ND
3.14
D
ND
ND
0.91
Orange
L
0.01
ND
9.43
D
ND
ND
1.05
White
L
0.03
ND
1.16
D
ND
ND
0.96
Yellow
L
0.01
ND
9.70
D
ND
ND
0.95
    L:  Light
    D:  Dark
              Table 5.3  Results of Leaching Test for
                         Heavy Metals in Colored Papers
                                                               (PPM)

Hg
Cd
As
Pb
Cr
Green
L
ND
ND
0.011
ND
ND
D
ND
ND
0.010
ND
ND
Blue
L
ND
ND
ND
ND
ND
D
ND
ND
ND
ND
ND
Red
L
0.0006
ND
ND.
ND
ND
D
ND
ND
0.011
ND
ND
Orange
L
ND
ND
ND
ND
ND
D
ND
ND
ND
ND
ND
White
L
ND
ND
ND
ND
ND
D
ND
ND
0.008
ND
ND
Yellow
L
ND
ND
0.012
ND
ND
D
ND
ND
ND
ND
ND
L:  Light
D:  Dark
      Table 5.4  Content of Heavy Metals in Combustible Waste
                                                    (PPM)

Hg
Cd
As
Pb
Zn
No. 1
0.20
0.2
<0.5
<1
174
No. 2
0.18
0.1
<0.5
<1
67.8
No. 3
0.53
0.2
<0.5
<1
59.6
No. 4
0.35
0.3
<0.5
<1
113
No. 5
6.20
<0.1
<0.5
<1
428
                                - 13 -

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                                                                  321
           composting system with incineration or other disposal methods
           without consideration of the local demand for composted
           material.  Composting system can be considered favourably as
           a good organic fertilizer which may be demanded by local com-
           munities.  If a good local market for composted material
           exists, those will be sold and revenue will partially offset
           the operation cost and net cost should be compared with in-
           cineration or other disposal systems.

5.  The Design of Separation System for Hazardous Material
    5.1  General
         Studies were conducted concerning on (1) how much the heavy
         metals are contained in domestic waste, (2) how to remove this
         type of hazardous material or glasses,  (3)  effect of separa-
         tion collection, (4) how about mechanical separation is.

    5.2  Content of hazardous materials (mainly heavy metals) in
         raw refuse
         The results of analysis are shown in table  5.1 which shows
         the heavy metals and PCB in combustible waste, paper, leaves,
         fruits, fruit vegetables,  tea, rice, meat,  fish,  and seeds.
         From this investigation, it can be said that the  heavy metals
         in raw refuse are not so much as being worried about, even
         though these materials become composted materials, and the
         possibility that contents  of heavy metals exceed  the temporary
         standard which was set by  the Ministry  of Agriculture is  very
         high.   However,  if the raw refuse which contains  cans is
         utilized for composting system,  some of the heavy metals  in
         the waste after shredding  exceed the temporary set standard.
         This is the important finding.

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                                                               322
5.3  Effect of the separation collection
     It can be said that the separation collection is good enough
     to remove the most of hazardous and toxic materials from
     composting system and it may be the most economical way to
     remove those effectively.  Here,  the various separation col-
     lection methods were investigated to see the degree of co-
     operation of householders and the degree of impurity in the
     waste.  The table indicates separation methods namely 2 kind,
     3 kind, or 4 kind -materials separation.  This table also
     shows what kind of materials are  separately collected, efficiency
     of separation and major items of  inpurities.  Summarize from
     this table is as follows.
     (1)  The efficiency of separate collection for combustible
         waste is about 90% on wet basis.   The separation efficiency
         is almost same for 2 kind, 3  kind,  or 4 kind separations.
     (2)  The efficiency is quite different and depends on whether
         combustible waste include plastics  or not.   Plastic
         materials are utilized in different products and in
         different ways.
     (3)  The separation efficiency for noncombustible waste is
         different by city to city (50.6%  to 95.3%).
     (4)  Major items of impurities are plastics and  papers.   It
         may be understood because these materials are utilized
         as carrying bags.   It is too  early  to make  any conclusion
         at this time,  but contamination of  glasses  and metals
         which are unsuitable for composting will be  about 10% on
         dry basis with any type of separation collection.   If the
         separation collection is employed for composting system,
         the 2 kind separation is good enough.
                           -  15 -

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                                                        323
Table 5.5  Comparisons of Separation Effects of
           Different Separation Collections

2 kinds
separation
3 kinds
separation
4 kinds
separation
Town
City
SA
City
HI
City
HA
City
KU
City
KA
City
KU
City
FU
City
AG
City
OK

Material
comb.
non-comb .
comb .
non-comb .
comb.
non-comb .
comb.
non-comb .
comb.
non-comb . (1)
non-comb. (2)
comb.
non-comb. (1)
non-comb . (2)
comb.
non-comb. (1)
non-comb . (2)
comb.
non-comb. (1)
non-comb. (2)
non-comb . (3)
comb.
non-comb . (1)
non-comb. (2)
non-comb. (3)
Materials
to be collected
normal comb .
metals, glasses,
ceramics, plastics
normal comb .
metals, glasses,
ceramics, plastics
normal comb . , plastics
metals, glasses,
ceramics
normal comb., plastics
metals, glasses,
ceramics
normal comb. .plastics
in kitchen
metals
glasses,
large plastics, ash
normal comb .
metals, glasses,
ceramics
plastics, rubber, ash
normal comb .
metals, glasses,
ceramics
plastics, rubber
normal comb .
metals
glasses
plastics, rubber, ash,
ceramics
normal comb .
metals
glasses
plastics, rubber, ash,
ceramics
Effect of
separation
(wet basis, %)
87.6%
94.4%
90.2%
79.4%
94.9%
68.3%
97.0%
59.5%
96.5%
94.3%
95.3%
91.4%
85.7%
50.6%
76.3%
89.7%
84.1%
91.6%
85.0%
80.4%
72.8%
92.6%
79.4%
75.4%
70.3%
Major items of
contaminants
plastics (12. 2%)
paper ( 5.3%)
plastics ( 5.6%)
paper (10.9%)
glasses ( 2.8%)
paper ( 1.6%)
metals ( 1.2%)
plastics(27.3S)
glasses ( 1.9%)
comb. ( 5.6%)
comb. ( 2.5%)
glasses ( 1.6%)
plastics (10. 3%)
metals,
glasses (44.4%)
metals,
glasses (15.6%)
paper ( 7.6%)
ash (10.2%)
plastics ( 6.5%)
comb. ( 7.7%)
plastics(10.2%)
comb. (13.8%)
plastics( 4.7%)
plastics(10.1%)
metals (12.7%)
metals (13.4%)
                     - 16 -

-------
                                                                    3?4
5.4  Investigation on the effect of separation techniques
5.4.1  Objection
       Some kinds of separation techniques are applied for the
       existing composting systems.  The object of this study is
       to investigate how much of contaminants remain after
       separation.

5.4.2  Contaminants and composting system
       For composting plants for investigation, the contaminants
       in the final product were analyzed and tabulated.  Contents
       of glasses, metals, plastics, wood, and other contaminants
       were measured for 4 major different cities.  The total
       contents of contaminants in these final products are 2.2 to
       5.6% in these 4 cities.  The recognized items are paper,
       match wood, chopstick, cigarette filters and human hairs.
       Two cities which use hand separation contains less con-
       taminants in final product.  It suggests something important.

5.4.3  Operation of separation
       From our investigation, it is said that the finer the
       particle, the more difficult to separate the contaminants,
       it is better to remove those in early stages hopefully before
       fine grinding.
                            -  17 -

-------
                                                       325
Table 5.6  Contaminants in the Product (%)

City T
City N
City H
City S
Glasses
0
0.9
0.8
2.2
Metals
0
0.5
0
0
Plastics
0.5
0.5
2.4
1.8
Wood
0.5
0.4
1.3
0.7
Other
Contaminants
1.9
0.3
1.1
0.8
Total
2.9
2.6
5.6
5.5
                   -  18  -

-------
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                                                                                 -   19   -

-------
                                                                     327
                            Composting System
                 Discussion Leader:  Dr. Sachiho Naito
Question:  At existing composting plants, how is the compost utilized?

           Is it primarily used on agricultural land or is some used

           by homeowners?

Answer:    I am a sanitary engineer so I am not so familiar with the

           agricultural purposes.  However, presumably the compost is

           used on farming land.  Hypothetically, it is also used by

           homeowners, but the numbers are negligible.  G-olf courses in

           Japan use it, for example.

Question:  U.S. interest in composting is presently directed mainly at

           composting sewage sludge without municipal refuse added.  Do

           existing composting plants utilize only municipal refuse or

           is night soil or sewage sludge included?

Answer:    Existing composting plants, according to the national census of

           the Japanese government, is utilizing only municipal refuse.

           There will be numerous difficulties of application of sewage

           sludge for the farmers, because of the heavy metals from

           industrial waste which are mixed with domestic sewage.   Un-

           fortunately, however, our data on sewage sludge is limited.

Question:  Is the SHIGENKA Center completed and in full operation?

Answer:    I guess our Chairman knows about this in detail—from its

           commencement to its completion.   It was begun last year, 1978,

           and I presume we expect full operation in 1980.

Question:  The Toyohashi City composting plant has been in operation

           since 1964.  Does all of the compost go to agricultural land?

           Is it sold or given away.

-------
Answer:    I guess composting must be used primarily for agricultural




           use.  I'm not sure if it is sold,  but if it is, it has no




           meaning so far as the coverage or maintenance is concerned.




           In other words, we are not concerned about the selling




           price as far as the operation is concerned.




Question:  The Toyohashi City .omposting facility relies on household




           sorting and classification of refuse.  Was this concept




           difficult to implement and how was it accomplished.  Does




           the collection truck have several compartments or are




           separate collections made?




Answer:    As we discussed and Mr.  TanaHa has articulated, collection




           classification of refuse depends on the close cooperation of




           housekeepers.  It was not so easy, but it has now been




           successfully implemented in our country.   However, I am




           doubtful about its implementation in the  United States




           because of the different system, and custom.  About the




           question of the collection truck,  according to my memory,




           packer-type trucks are still very popular in our municipalities.




           But, dump trucks are becoming more popular than ever—more




           than the packer-type trucks as collection vehicles.  As




           far as resource recovery is concerned the dump truck is




           better than, the others.




Question:  Most U.S. sewage sludge composting operations consist of 21




           days of composting followed by 30 to 60 days of storage to




           further reduce odors.  The new SHIGENKA composting operation




           consists of three stages:

-------
           1.  rotary drum digester - 1 to 2 days




           2.  multistage digestor  - 3 days




           3.  maturing area  - 5 to 7 days




           Total composting time therefore is 9 to 12 days.  Does




           this result in sufficient stabilization to eliminate odors?




Answer:    Thi:; is a very delicate question.   I guess specialists




           continually debate the issue related to odors and stabili-




           sations.  It 7'-' certain that the longer the duration of the




           "tabilization,  the more the elimination of odors is achieved.




           Theoretically 9 to 12 days of composting will be enough to




           cover overall odor elimination throughout the composition.




           But, the odor problems should be discussed from other angles




           as well.  For instance the very sensitive Japanese design




           shows a complete close-file system in which all of the odors




           will be collected by means of ducts which are placed through-




           out the system.   All  odors collected by these facilities will




           be treated through the compost in order to eliminate the odor




           source by means of biological reactions.  Then the compost




           will be able to substitute activated carbon.








Question:  What is the reason that you are moving away from the packer




           truck to the dump truck?





Answer:    I guess the main reason is the source of the  garbage.   If you




           use the packer type,  some of the impurities may get into the




           refuse.   So after the refuse is taken out of the packer trucks




           separation of the waste is very difficult.

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                                                                 330
Question:  Did you say that you are not composting municipal sewage




           sludge and that you are just composting solid waste?




Answer:    This is another hard question for me.   For instance, the




           EPA of the Japanese Government has never developed an agree-




           ment with the sewage operators.   About 90% of the sludges




           will meet the criteria which the Minister of Agriculture




           has established; so this is accepted.




Question:  How do you do all this separation of batteries, plastics, etc.?




           Is this done by hand?  By the homeowner before it goes into




           the garbage can?




Answer:    Hand sorting mast be used.   However, we are now conducting




           a pilot study on how to separate the garbage with sophisti-




           cated technologies.  We are hopeful that this technology can




           be used in the future, but  at present, the majority of the




           separation is by hand.  We  have estimates of how many  bat-




           teries are contained in our waste.  Presently there are 10




           batteries in one ton of waste.  We computed this figure from




           sales volume of batteries versus production of waste.




Comment:   I just have one comment.  The situation in the United States




           probably is just the reverse of what Dr. Naito explained was




           occurring in Japan.  All of our municipal refuse composting




           plants have closed down.  We had a number of them in the




           1960's and early 1970's and all were very unsuccessful.




           But we have a considerable  interest in the larger application




           of the municipal sewage sludge composting.

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                                                                    331
Comment:   I might add to that that there are two operations that we




           know of that are continuing composting.   New York uses the




           waste from nearby vegetable and fruit markets and combines




           it with leaf collection.  The other one,  Bangor,  Maine,




           composts tree trimmings, side agricultural wastes and




           domestic waste materials.  But neither of them is using




           municipal solid waste.




Comment:   I'd like to give you an up-date on this  subject as well.




           Beginning in 1978,  four municipalities  in Japan  are




           considering construction of composting sites.   And for




           sewage sludge composting, that's under the jurisdiction




           of the Ministry of Construction and they are working




           on it.

-------
                                                 333
4  Resource  .Recovery  Tcdmolojrirs
   4 — 3 'Modem. Composting  Syslein(2)
             TOYOJIASlll   CITY





      Urban  and   Rural   Environmental



      Combiiwt i on  System
                     My









           Sliijjvni  Aoki




           Mayor, Toyoliashi  City

-------
                                                        334
                           Contents





1.  Forevord	   2



2.  History and  Intention of URECS1 Project   	   2



  2-1.  History	    2



  2-2.  Intention	   6


                                 *2
3.  Rough description of SHIGENKA  Center   	   7



  3-1.  Overall  project  	   7



  3-2.  Features of SHIGENKA Center  	  13



  3-3-  Matching of the agriculture	14



  3-4.  Operation and Management	17



4.  Compost Planning 	  19



  4-1.  Separation Collection  	  19



  4-2.  Composition, and Amount of the Object  of  ....  21

        Treatment



  4-3.  Treatment System 	  23



  4-4.  Effect of the Products	2o



  4-5.  Features of this Project	28



3-  Conclusion	  33
 Note:



  *1 Abbr. of Urban and Rural Environmental Combination System



  *2 Proper noun of Waste treatment and Resource Recovery Center
                         -I-

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1.   Foreword
     Our city, Toyohashi,  is  located practically at  the  center
of Japan.  The city  is  favored with its  traditions brought  up
by the variegated occasions in its long  historical existence.
It is continuing at  present the  spectacular  development  as  one
of the key cities for the  development  in the Chubu (Central)
Region of Japan.
     The formation of an ever novel and  yet  harmonized city
is bein.000  households  or  so
       Population                  300,000 or so

2.    History and Intention of UREC3 Project
  2-1  History
     The volume of wastes  discharged from  a  city is  showing an
ever increasing- tendency year after year  in  addition  to  the
wider multiplification of  the types of the waste because of the
over increasing growth rate of economy and the  improvesent  of
the way of living.   So,  the proper v.ay of  the treatment  of  the
nbran waste and the consolidation of the equipments  for  its
treatment are now becoming ono of the major  problems  common to
all the cities in Jaoan.
                              -2-

-------
     On the other hand,  there  is  a  cry  warning the limited




amount of the resources  available on  the  earth globe on the




large worldwide viewpoint.  So, the study and investigation




are getting at present under way  for  the  method of leaving as




large amount of these resources as  possible  to our offspring.




     The optimum treatment and utilization of waste has appeared




under the limelight as one of  the major problems in front of




such background as described above, and the  administration for




cleaning work suitable for each of  the  cities including the




reduction of the waste amount and the resource recovery from




the waste is appearing so as to be  taked  shape.




     Since 1964, the composting equipment has been already ope-




rated in our Toyohashi City with  the aim  of  establishing new




administration of cleaning v.ork corresponding with these require-




ments of modern society.  In the  year 1970,  however,  "Committee




for the investigation of the measure for  the integrated treat-




ment of urban waste " was inaugurated in  the City Government




aiming at the further investigation of  the problem on the basis




Of the said equipment.  As the result of  the research and in-




vestigation carried out by this Commission on the existing




state and the future countermeasure against  the  problems confront-




ing this city, "Concept of recurrence to  nature  in urban and




rural districts" was prepared in  1973'  As to the phase of the




promotion of rural districts, on  the other hand,  "Council for




the Drorrotion of integrated readjustment  of  rural districts" was




inaugurated in the vast area of agricultural villages in the




southern part of the City, and the  new  "Concert  for construct-




ing a nodcl development of agricultural production utilizing1




the energy of waste heat" w,-*s proposed.   Lastly,  "Pi'ojoct for
                         -3-

-------
integrated  demonstration of readjustment of the environmental




conditions  in  urban and rural  areas" was established in 197^-




     The  council  for promoting the integrated readjustment of




rural  districts,  working- as the on-the-site or£einization of




these  projects , executed the adjusting uork on the site.  As




tbo  result,  the projects for "Vork for environmental read-




justment  of live-stock breeding" and  "Work f o c integrated read-




justment  of rural equipments"  vere established and approved by




the  Ministry of Aost processing




and  the utilization of  waste heat all of which satisfy the




existing  conditions  required for the objects of subsidies for




the  readjustment  vorks  of  equipments for refuse disposal in




addition,  to  other equipments for utilization (heat recycling




equipment arid  so  on)  in terms  of the pilot  work of the said




pro j ec t .




     As describee1  above, the related agricultural \orks vere




started in  1975 followed by the work of tho integrated resource




recovery and was to  treatment vhlch  was started in 1977-  At pre-




sent, we are endeavoring to promote the project with the utmost
                               -k-

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Fig. 1.  Structure and expenditures of UHECS Project
Urban and
Rural En-
vironmen-
tal Com-
bination
System
(URECS)
 10,032,748
(in t:iou-
 sand Yen)
               Works controlled
               by Ministry of
               Health and Wel-
               fare
                8,584,000 (in
               thousand Yen)
               Works controlled
               by Ministry of
               Agriculture and
               Marine Products
                1,443,748 (in
               thousand Yen)
Works of the integrated
resource recavery and waste
treatment

Plants for treatment
Planb for utilization

Construction of SHIGENXA
Center
 8,584,000 (in thousand Yen)
Works of integrated read-
justment of rural equipments
and the secondary work of
improvement of agricultural
structure

Construction of Training
center
 260,000 (in thousand Yen)

Construction of vegetable
hothouses development
 671,404 (in thousand Yen)
Works of environmental re-
adjustment of live-stock
breeding

Meadow forrii.ng work
 396,344 (in thousand Yen)

Works of live-stock
dropoings trarisporation
nach Lnery
 11,000 (in thousand Yen)

Fowl droppings drying
wo rks
 110,000 (in thousand Yen)
                               -5-

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   2-2.  Intention

     An optimum treatment  of  waste  is  one  of the major problems

confronting the urban administration^  This  work intends to pro-

mote a cleaning administration  of novel  type by which the thermal

enerpy or the organic compost generated  from the urban waste is

recycled to agricultural areas  with the  result  of accomplishing

the environmental readjustment  of a city and the pronotion of

agricultural industry at a same time accompanied by the recycling

utilization of those useful elements included in the urban waste.

The major points of this project are listed  below.

     (l)  Optimum treatment of  waste

          Optimum treatment of  waste for the purpose of protect-

          ing the environmentc

     (2)  Effective utilization of  waste

          The heat generated  by incineration is  used for the heat-

          ing of vegetable hothouse and  for  the  hot water supply

          to the Training (such as  cooking, gymnastics)  center as

          well as for generating electricity to  be  used within

          the plant as a part of their electricity  consumption.

          The waste compost is  returned  to agricultural area.

          The metallic materials, glass, and  so  on  are  recycled

          ar. the resources.

     (3)  Refuse and waste disposal combined  with promotion
          of agricultural industry

          The rep-ional agriculture  is pro.r.oted by supply 0T heat

          to vegetable hothouses, recycle  of compost to the agricul-

          tural area,  treatment of  live-stock droppings  and  so on.

     (.'>)  Ratioruilized integrated treatment  niants

          Tho costs required  for construction as well as  Mainte-

          nance and operation arc alleviated bv  rationalized
                              -6-

-------
           design of an  integrated  system combining the plants




           operated for  various  purposes.




      (5)  Integrated  control  of the  plants




           Concentrated  control  is  operated  as an integrated




           plant for treatment with the  result of optimizing




           the maintenance and control as  well as alleviating




           the expenditure.




      (6)  Overall countermeasure for environmental protection




           Utmost attention  is paid for  the  environmental protec-




           tion including the  atmosphere,  water,  offensive smell,




           noise, vibration  and  so  on, all of which are controlled




           in such a way that  not only the values prescribed by




           the existing  regulations are  satisfied,  but  also




           severer values may  be accomplished.




           The layout and the  structure  of the equipments will




           be determined to  conform with the environmental condi-




           tions of the areas.  Trees will be planted and other




           measure for environmental  protection will be executed.




      (7)  Establishment of  the  system of  separation collection




           The system of separation collection of waste will be




           established for the purpose of  optimum treatment




           of waste.




           The road traffic  environment  will be protected by




           designating the road  for waste  transportation and




           avoiding congestion of refuse collecting vans.




3.   Rough description of SlilGENKA  Center




   3-1.   Overall project




     The resource recovery and vastc  treatment center vhLch




forms the core o*~ the URECS  project comprises the follo'.-'ing
                              -7-

-------
 five plants:  Incinerator  plant,  High-speed Composting  plant

 Night Soil Treatment  plant,  Resource Recovery Plant  (equipped

 with Crushing and Variable matter separation systeir.) and

 Fowl Droppings Drying plant.

      Waste of various  types  are  carried into this SHIGENKA

 center for the purpose of  disposal and recycling treatment.

 Fig 2 shous the conceptual sketch of URECS project.


      Fig 1  Conceptual sketch  of  URECS project
Urban /
refuse j
u o
i
i
Office type
refuse i
( Comous-
tibles) ]
1
Night soil

&-J ]}
Live-stock
dropoings
<5=3 — ~J
Valuable matte]
r__jg 	
Bulky refuse
r=ri 1
	 	 . ^ . > X,
Electricity j ; Vegetable/// / Training
generation ' 1 hothouse/vS's. ' center
within equip- j ^ f
ment ~~ [ |
Agrucultural [_
; area
Incinerator _ , T^T 'l^-^''
1 plant [ "t:*"i -^^^s '-''''
J_.. ^
! High-speed comnost- |
| ing plant |
P
_L > Nig-ht soil treatmentl • ,
i i olarit 	 1 H \ Market
tJ- L. jt
r Resource Recovery] ' i, i
olant (Crushing &j ' '' .
._ > Separation) i
I ; j
Fo-.. 1
                        	 t    \ator used  for
            Fo-v.l c'rojipings j ;    mo^dov  ant'  tree
            jdrying plant	j |"".'  planting
',;''/.-:..
                                               (Ash  contents  etc.)
                                               u^ed  for  lanr1  reclama
                                               tion  (treatment  yard)

                                               (Clarified  vntcr,1
                                               c. ischux ged  into  river.

-------
     As you see in the sketch, of the refuses classified  and




transported into the waste treatment plant,  those  of  combustible




nature, bulky refuse, refuse used by recycling, and toxic




waste are mixed with those generated from  other plants  inside  the




recycling center - co-.r.post residue discharged from the  high-speed




speed composting plant, combustibles selected at  the  Resource reco-




very plant, residue discharged from the pre-processing  of the




night soil treatment, and so on - in an optional manner for




the purpose of incineration.  The heat energy is recovered in




the form of steam for the heating of the vegetable hothouse  or




for the electricity generation.  On the other hand, a part of




the combustible waste is mixed with the live-stock droppings




and the c'esiccated sludge discharged by the  night  soil  treatment




plant producing compost of good quality.   As to the night soil




treatment, the crude night soil, the sludge  deposited in  the




purification tank, and the live-stock droppings are treated  in




a perfect manner so that a part of the treatment water  is




recycled by the  SHIGENKA center as the plant water*  As  to




the Resource recovery plant, iron, aluminium, glass and so on




are recovered for the recycling purpose.   As to the fovl  dropp-




ings drying plant, the fowl droppings are  dryed and used  as




the fertilizer.




     As described above, one of the features of this  center  is




that refuses of various types are treated  in such  a vay that




they are recovered in the forms of corr.nost,  valuable  matter,




sunoly water and other various typos of resources.




     Follovinr is the description of the technical items  of




the plant.




    3-1-1  Incinerator Plant




     Mean nixing rate of various types of  refuse treated  in




                              -9-

-------
the incinerator  is  as  follows.

     Household refuse  (combustible refuse)    129ton/day

     Combustible refuse  discharged from       85ton/day
                                offices

     Bulky refuse and  combustible  refuse      13ton/day
      discharged fror...  the  resource recovery plant

     Residue discharged  from night soil        Iton/day
      treatment  plant

     Conpost residue                           33ton/day

     The major composition of this system is as follows.

Incinerator              Mitsubishi-Martin system

                         Capacity:   l4yton/day x 2 vrnits

haste heat boiler        Maximum evaporation volume:   12 ton/day
                                                        >x 2 units

                         Steam temperature:   250 C
                                                      2
                         Steam pressure   :   2O kg/cm g
                                                       o
Electric precipitator    Maxirr-um gas volume:  24,500 Nm /h x 2 units
                                                           o
                         Soots  and dust at  outlet: O.lg/Nm
HCI and SO  removing device                  2 units
          x
                                                       o
                         Maximum gas volume:   24,500Xm /h

                         IICI at outlet      :   90ng/Nm3

                         SO  at outlet      :   50 ppm

l.aste heat utilizing     Steam turbine  type electricity generator
 device
                           (Rating:  1,500 kW)    1 unit

                         Heat supplying equipment (Steam
                           accumulator and auxiliary boiler
                                               each 2 units)

     As described above, a partiou]ar consideration for the

protection of environment  from a secondary  pollution is paid

by the waste treatment and the  resource recovery from \\aste.

     The operation  of  the  incinerator is continued practically

arotmr' the cJock.   So, various  typos of automatic control

devices are installed  for  the control of the incineration

                               -10-

-------
amount of refuse  and  the  voluue  of evaporation as well as
the control of  the  gas  temperature at  the outlet of the
incinerator.
     3-1-2  High-speed  composting plant
     The mixing rate  of the  wastes treated by this plant
and other major technical items  are as follows.
     Household refuse                82 ton/day
     Live-stock droppings           l'-4 ton/day
     Desiccated night soil sludge   ik ton/day
     High-speed compost plant        Fuji's High  speed compost
                                     system
                                     Capacity:  64ton/day x 2 units
     As to the treatment  process  of the  high speed composting
plant, the detailed description  will be  given in the para-
graph ft-3-
     As to the operating  hours,  the crushing is  operated for
6 hours, while the aeration  and  so on during the digesting
process is operated continually  around the clock.
     The mo.st important features  of this  system  are that the
initial and the ma i.n digesting process is operated in con-
tinuation by the mechanical  procedure and that the diffusion
of offensive smell is prevented by sucking the air at the smell
source„  Further,  the selecting devices  of three steps are also
installed for the purpose of improving the product value of
t •!£ compos t.
     3-1-3  Night soi. 1.  treatment  plant
     The mixing rate of the  wastes  treated by this plant
an~ other ina.ior technical items ai"e as follows.
     Crude n i f h t soil               1'tl k  (, /day
     Sludfo of clarifying tank       -40 k  (/day
     Live-stock droppings            12 k
                             -II-

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      Night ?oil treatment plant:     Mitsubishi high-speed night
                                      soil oxidization treatment
                                      system

                                   Capacity:  243 kl/riay x 1 unit

      The vasto vater and so  on  venerated in jind discharged

 from SHIGENKA center is  also treated by this  plant...  This plant

 Hdopts tho aniiiioii iiim stripping process  for the de-nitration, and

 UOD,  SS, CCD and so on are relieved  by  the aeration process,

 tie  coagulating sedimentation process  and so on.

      The treated wo.ter is processed by the  high degree treat-

 n ent  method,  and it is scheduled  to recycle about 500 kd of the

 troetted vater as the cooling water  for the  machinery and other

 miscellaneous uses.  The remaining  part of  the treated vater

 is discharged into the river.

      Further, a large volume of dilute water is generally

 required for  the treatment of nirrht  soil,,   According to this

 project,  however,  the water- saving  system is adopted by re-

 cLrculatinfr the treated v,-ater within the  plant.

      3-1-4  Resource Recovery (Crushing and Separation) Plant

      The volume of waste  classified  ond  transported  into the

 Resource Recovery plant  is 8 ton/day of bulky  waste and  52  ton/day

 of resource refuse.

      Bottles,  aluminium cans, and so on are recovered  from

 t'ne refuse  by r.anuel selection in this  plant.   As to regaining

 nrrt  of  the refuse, it  is crushed in smaller size anr'  classified

 into  the  iron,  ccirbu.s tible ,  and incombustible  by the meche.nical

selector.

     Bv  the ••••oy , dry batteries,  fluorescent  3ai.:p-., ? nd  other

  toxic   el crr.cn ts  are  also  rrr over', by  the  process o

c election.


-------
They are sealed in concrete vessels and disposed  by the landfil




     3-1-5  Fowl droppings drying plant




     The volume of fowl droppings treated  by this plant is




10 ton/day.




     The fovl droppings drying plant comprises  the primary




and the secondary processes.  At the primary process,  the low




temperature drying process is carried out  by means of  the




electric energy generated by the independent generator of the




olant for the purpose of preventing- generation  of offensive




3n;ell.  As to the secondary process, the drving system by




rreans of the kerosene is used aiming at reducing  the moisture




content of the product to 13% or so.




     By the kerosene dryer described above,  the air used by




the kerosene for drying process is sucked  frorr  the location




'..'here the offensive snell is generated.




   3-2  Features of the SHIGENKA center




     3-2-1 Organic combination of equipments




     Each of the plant generates at its treatment process the




secondary discharge described below.




     (incinerator plant):  Plant drain water, incineration ash




     (High-speed composting plant):  Compost residue,  filthy water




     (Night soil treatment plant):  Sludge,  offensive  air,




                                    night  soil  residue.




     (Resource recovery plant):  Combustible refuse




     (Fowl dropnings drying plant):  Filthy  water




     All of the discharges listed above may  not be cast away




as they are excepting the incineration ash.   As a rule, there-




fore it is necessary to nrovide tho treatment plant for these




discharges.  By tV.is project, however, they  are perfectly
                              -13-

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processed inside  the  center without  installing a treatment




plant inparticular by utilizing the  mechanism of organic




processing function of the  integrated  waste treatment center.




     For example, the compost  residue  and the combustible




waste are burnt in the incinerator in  combination with the




air with offensive smell, while the  sludge is made into




ccmnost for the recycling and  the  filthy water is processed




by the night soil treatment plant.




     By the vay,  the  back up system  is also established so that




each of the plants may be operated independently with the aim




of assuring the environmental  protection when the organic




combination of the plant develops  unbalance.




     3-2-2  Energy saving and  resource saving project




     Electricity  is generated  by the turbine  generator at the




incinerator plant so  that a large  part of the electricity




consumed in the center is supplied by  its proper hand.




     The system of night soil  treatment plant requiring




only a small volume of dilute  water  is adopted*   In addition,




the treated water is  recycled  for  the  use inside the center




for the rmrpose of reducing- the water  consumption of the center.




   3-3  Matching  of the agriculture




     Various types of resources are  recovered by this resource




recovery and waste treatment center.




     (incinerator plant):   Thermal energy (steatr.) and electricity




     (lILgh speed  composting plant):  Cornnost




     (Night soj1  treatment  plant):   Supply water




     (Resource recovery plant):  Iron,  aluminium, glass




     (Fovl dronnin/.s  drying nlant) :  Fowl ciroprvings




     Of the recovered  losourccs Its tod  above,  the total volume




of the electricity and  the  supply water is consumed in the center




                               -14-

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for  its proper purpose.


     As to  the iron, aluminium,  glass and  so  on,  manufacturers


of each of  the materials  carry  them away.   They are  reprocessed


by their hand and placed  on  the  market  for the  second  time.


     As to  the remaining  steani,  con.post, and  fowl droppings,


they are recycled on the  agricultural area.   The  route of cir-


culation (users) is already  established for the compost and


so on.  It  is believed that  the  scope of utilization iifill


further increase when the quality of the products makes a


further ir.vproveivent in the future.


     Next,  let us describe the steam, it is already  designed


at the construction of SHIGENKA  Center  that the steam  generated


at the center can be supplied to the vegetable  hothouse develop-

                o
ment of 4U,000 m  or so in the vicinity of the  center  all the


year round.  Therefore, the problem of  the  stabilized  supply


of steam is one of the most important items of  this  project.


     The concrete details of the design are shown in Fig 3-


In other words, the amount of steam required  by the  hothouses


makes a conspicuous fluctuation  according  to  the  atmospheric


temperature.  On the side of the center, on the other  hand,


the steam load of the vegetable hothouses  is  equalized by


installing  the steam accumulator.  Further, the amount of steam


supplied by the incinerator will be in shortage when a low


temperature condition of the atmospheric tomoerature continues


for a lonf  time.   So,  tvo units of auxiliary  boilers (evapora-


tion volume: lOton/h'r) operated by kerosene  burning system  are


also installer1.  In addition, considering  the caso of  service


interruption of the con;nercial electricity, a syster.*. is also


provided by vhich the sunply of steam is continued by  operating
                              -15-

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the auxiliary boilers by the diesel engine generator.
Fig T.  Stabilized steam supnly to vegetable hothouses
Boiler operated
by wasto heat
from incinerator
Auxiliary bojlor
(operated by ke-
rosene)
(At norrral operation)
    1.
                      Steam ac-
                      cumlator
                          Supplied to
                          vegetable
                          hothouse
(Back up steam supply)
             (Pover supnly at service interruption)
          _L
Diesel engine generator
                              -16-

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   3-4  Operation and Management




The operation and management of SHIGENKA Center is based upon




the concept of efficient recovery and effective utilization




of the resources by their optiir.um and perfect treatment




after they are transported into the center.  Further, it




always aims at the reduction of the secondary pollution and




the perfect protection of environmental conditions.




The indispensable requirement for the plant operation is




to construct an plant of integrated treatment combining each




of the eouipments in an organic manner.  The transportation




and treatment are operated in an integrated manner and the ope-




ration control as well as the devices supervising the environ-




mental pollution and the laboratory installed inside the plant




are always actively operated so that the operation is controlled




according to the result of the supervising activities.




The plants of the preprocessing and the auxiliary nature are




operated 5 or 6 hours daily because of their functions and




particular characteristics.  Hovever, the major plants includ-



ing incinerator,  nifht soil treatment,  high-speed composting




plant are operated around the clock in continuation.




The personnel distribution is shown in Table 1.  The number




of personnel is 95 which includes technical personnel with




approved skill for each of the particular fields.
                              -17-

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Overall
management

13 personnel
                  '  Central
                  j  supervising

                    32 personnel
                                      Incinerator plant

                                      9 operators  29^tori/day
                      High-speed composting plant

                      5 operators  128ton/day
Maintenance
and management

9 personnel
Analysis
nanagement

2 personael
                     • Nighfc soil treatment
                    J ipiant

                      7 operators  2kj k fi/day
   Resource recovery plant  I
I	                          '
l  I                     .     |
l   12 operators  goton/day  j
i  I	•	'
                                   u
                      Fowl droppings drying
                      plant

                      4 operators   1Oton/day
     Table 1.  The personnel distribution in Center
                             -IS-

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4.  Compost Planning




  4-1  Separation Collection




     From the standpoints of resource and energysaving,




refuses is collected using a. four-division "Station Collecting




System" with collections scheduled for the sarre day each  week




and collecting area divisions corresponding  to elementary




school area divisions.




     After further investigations of "Collecting Frequencys




and Carrying Method Factors" the present four-divisions




(refuse, hazardous materials, bulky refuse,  toxic materials)




will be increased to Five (the previous four D!US one for




valuable refuse).  The station collecting system will not




be changed.
                             -19-

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        Table 2   Refuse sorting and treatment

                 Sorting

Garbage
Cooking was te ,
food, peelings
f* £T'rc }-] £> 1 1 t; _
Co'.nbus t ible
(Refuse)
                A«as te-
                paper

                V.ood
                         fishbones, etc.
                         Tissue, pa'oer scraps,
                         paper cups ,  etc .
                         V.aste boards & planks,
                         sticks, bamboo, twigs,
                         etc .
                        i	^	__
Noneonbustible
(Hazardous
material)
Valuable
r.iatter
Bui cy refuse
Toxic waste
(toxic
 materials)
                 Ceramics Bowls, plates, flower-
                         pots, vases, cosmetic
                         containers, bottles,
                         etc.
                 Plas
                 tics
               h~
                 Others
                 Glass
                 Metal
                 Old
                 paper
!Vinyl wraopers,  polyethylene
 packages,  polyethylene
 tableware,  toys, stationery,
 styrere foam,  vinyl shoes
 &.  bags, etc.
 Leather goods, rubber goods,
 synthetic  fiber goods,
 ashes,  tiles,  pebbles, etc.

 Empty wine,  beer,  beverage
 &  whisky bottles,  medicine
 bottles, glass,  etc.
jEmpty wine,  beer & preserve
 tins,  iron & copoer scraps,
 etc.

 Old magazines  & newspapers,
 carton board waste, etc.
                 Textiles  Clothing, cotton, etc.
                                                         Treatment
                                Tncineration
                                Compos ting
                                                         Landfill
                                                        Reutilization
                                                        Incineration.
                                                        Landfill
                                                        Solidification
                                                        of toxie
                                                        vaste
                 Furni-
                 ture
                        Cabinets,  dressing tables,
                        desks,  chairs,  beds,
                        mattresses,  sliding doors,
                        glass doors,  kitchen
                        utensils,  etc.
                Electric T\7S,  radios,  refrigerators,'
                house-  sewing ;aachi.nes,  washing
                hold    machines,  foot  uari.-.ers,  etc.
                appli ances

               iVehicles Motorcycles, bicycles,  baby
               •         carriages,  tricycles,  etc.

                        Dry Batteries,  therinoineters,
                        f L'jorescerit  la.ips,  mirrors,
                        etc.                         ;
                                                         -  ditto  -
                                Solidification
                              -20-

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  k-2  Composition and Amount  of  the   Objects  of Treatment

     The volume of refuse discharged  and  collected from general

households, on the basis of a  monthly average  index of 1OO,

is highest in July, at 116, and lowest in February, at 8?.

(See Table 3)
        Table 3 Monthly index of  collected  refuse


                         I •» *
                                                         ,     :      i
> Month ' Jan.! Feb . j Mar. Apr.l May j June July .Aug.  Sept.  Oct.,' Nov. ' Dec .  j
 Indexi104   87
                 98
98 ,107! 100. 116
107   98  '  98 :  91  I 99
     The water content of refuse varies widely according to

season, ranging from a high of  71^>  to a  lov of 577°-   Therefore,

the specific gravity of refuse  also  changes  seasonally,  varying

between a high of 0.39 and a  lov of  0.3.

     Generally, in Japan, household  refuse  collected  in the

surrmer has high water content and an accordingly high specific

gravity.  In winter time refuse has  a lower  water content and

therefore a lower specific gravity.   This  trend is sobstantiated

by various data sources.

     In regard to live-stock  dropping, only  live-stock dropping

which has been separated into its solid component at  its

point of origin (cattle pen etc,) to delivered to the composting

plant for treatment.  Night soil sludge,  crude night  soil

sludge, and household septic  tank sludge  are delivered in the

form of desiccated cakes after  treatment  at  the appropriate

treatment plant.

     Physical characteristics of raterial  which can be treated

are shown in Table k (for refuse) and Table  5 (for live-stock

dropping and night soil sludge).
                             -21-

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w •

-------
      On this  basis,  the quantities of different  wastes  to be

 treated at  the  composting plant can be estimated as  shown belows:

      Table  7  Quantities of wastes to be  treated and  their

               respective water content        (Supply:  ton/day)

                                                (\vater content: fa)
      	 *!=-
        Qt.
Refuse i	j.-;;
               85   71   80
       ! ¥.cf   64165.5 57.1
1
5!
61
i
i
!J
8I
	 L_
9!
10 '
11
Live-  i_
.stock  |
jdropp-
          *1
         , *2
         . c .
 80  88; 82' 95,  88

672 ! 64.1 ^652 ;68.2 '71.0
    i - - ..    '    1
         14

         85
                                                80'  80  75 . 81
 Daily
j ayer.
 " 82~
                                               66.9! 66.2  64.3 ,63.4 |  65.2
                                                               7~l4~ "
                                                               ^_g_
          ,-•
        Qt.
Night
  ...
son 1
sludge '
Total
         " •
           *2
                                   14

                                   75
                                       14

                                       75
! * 1
i V.cfl 68.0 69.6
1 |
108
63.1
108
701
, 	 _ 1
116
679
-
110
69.0
123! 116
70.9 |73.2
108
70.3
108 i 103 Ti09
1 i
- "i ----p--
6 98 i 6 8.5 67.7
i 	 L _,
110
69
                                      Notes; *1.   Quantity

                                             *2.   Vater content


   4-3  Treatment  System

      General household  refuse,  night soil sludge from treatment

 plant, and. live-stock dropping from farms are mixed together and

 treated at high speed composting plant for speedy cor.vension

 into compost for  fertilization purposes.

      This system,  characterized by its high speed compos t i ng,

 uses the following steps:   reception and feeding,  crushing,

 digesting, sorting,  maturing,  and removal.  For  disestion,

 this system uses  three  types of digesters.  Primary digestion

 is carried out in a rotary c'rurn digester, and then passed to

 a multistage digester for  secondary digestion.   After pass-

 ing through these tvo digesting stages, the uaste is matured

 at the maturing area, where its compostable ingredients are:

 quickly converted into  usable  eorpost.

      A treatment  flow is shown  in Fig.  4.
                               _ 9 1_
                                £-.

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-24-

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      Toxic materials are  eliminated  by the preliminary sorting

 and classification system described  above.   Noncompostable

 materials in the refuse are  removed  by various  sorting machines

 as shown in Fig. 5.  The  remainder is  then suitable for pro-

 duction of high quality compost.

      Fig. 5  Types of sorting facilities
        Trommel

 Double trormel type
   Vibrating Screen
      Separator
     Balance type
Vivrating,
inclined-conveyor  type
                     £•                     <£ '
 Grain size: about 25 , Grain size: about 15 1
 For elimination of:  . For elimination of:  i For  elimination of:
 vinyl,  cloth, wood,  ivinyl particles,
                      i
 bamboo,  bottles,      glass particles,
                      i
                      i
 cans,  batteries,     i par>er, v:ood, bamboo
                      glass particles,vinyl

                      particles,  ceramic

                      particles,  pebbles etc.
 rubber,  cardboard

 etc.
etc .
               Raw    i
               compost
            v
                                                   FresU
                                                   compost
                                                            Fan
                                                             Fresh
                                                             CO(ll,)OS t
                                              Non-com _>ostable
         Raw  compost           Fresh compost
• Non-                  Non-                   compounds
; coMpo stable            com portable
: compounds
                       coi
                              -25-

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  4-^1  Effect of the Products




     In 1964, this municipality introduced a high speed




composting plant for treating waste in Toyohashi City.  Since




then, it has made a substantial contribution to local agricul-




tural production by supplying high quality compost for




fertilization.  On the basis of its experience, this municipality




has devised a new olan to systematically treat organic waste




in and outside the plant simultaneously with a combination




live-stock dropping and night soil sludge and household refuse




to improve overall composting efficiency.




     The resulting compost product, they feel,  provide an




improved fertilizing effect with a resulting improvement in




crop yield and duality.  To confirm the possible effects of




such a treatment system,  experiments were conducted.  Results




are shown in Table 8.
                             -26-

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Table - 8  Experimental Results of mJxing  treatment
Item
i N
Manure j
contents 1 Pp^N
K20
| CaO
MgO
Na00
i ^
C
H
i
Desiccated Laboratory
Pig dropping night soil ' scale
sludge compost
4.6 4.0 1.7
j
[ 7.27 9.01 1.82
T J
| 1.47 i 0.44 0»92
2.8 2.52 —
. i i
" ' !
j 1.67 j 1.74 —
] 0.59 0.59 —
| 42.0 35.7 30.4
6.5 5.4 _
Notes; Constituent values for pig dropping and desiccated night
soil sludge represent measurements prior to mixing.
Reference: Jaoan
tion,
Urban refuse I
cornpost 1 	
fff
rP
K
H
Environmental Sanitation Industry associa-
vaste Treatment Committee Guidelines
Toyohashi City
i;em Guideline j product at present
i
Sf 0.5 or above 0.71
O 0.2 or above O.68
— ,? i
O 0.25 or above 0.68
-
„() 40.0 or below —
2 |
                             -27-

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  4-5   Features of  this Project




     The  high speed composting plant of Toyohashi  City has




been in continuous operation since its completion  in 1964,




compiling a solid performance record and providing a substantial




contribution to loccil agriculture and municipal  sanitation.




     Contrary to the national tendency to prefer incineration




over- cor.poK ting for treatment of municipal refuses,  Toyohashi




City has  used the composting plant succes'- fully  for several years,




This i.3 probably because  the sorting-and-classif ication collec-




tion system,  on which the  supply of rai* material for convposting




c'cneiid.s ,  has  boen practiced  for several years vifa the ccn.plote




cooperation of local citizens.   In the physical  and chemical




Stan Jpo.irts ,  inconvenient  materials for ccnpostiiig- should be




elininated from the, vaste.   Their efforts have resulted in unique




treatment  facility st the  local v;aste plant.




    4-5-1   Digesting Facilities




   0 Rotary Drum Digester




     fj'icroot'ganisms which  grov  and function in the  rotary drum




         ,  the first digesting stage,  are classified as facultative
anaerobes  and aerobes.  Such bacteria is active betveen 30 C-45°C,




a ter.iperature reinge corresponding to that for inesophilic and




t?jor.Tiop>Li lie  bactorias.  Accordingly,  the atr-,osp>:ere  in the




difester  is acidic.  In thi.s digester,  fats, cai'bohydrates , and




wuf,;ir.-3 contained in oigatiic refuso  ore  dissolved and  digested




to .Torn uitldJc pi'odi.ic t'5 nnd cause a rapid proliferation of




bacteria.  T!i •  rcfu^f; kept  In  tliis  c'igc -.- tt-i for a iel;itively




•^cri-O ', n.oir.i.illy ctio or t\\c< days.




   0 Mu.l t i 5 t ;\ge D i g.vs t e r




     r.-i',. cori'no^t ^roc':ict>'j in tlio  rotary  drum < ' j ,", o «- 1 e i- is
                          -28-

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delivered  to the next digestion stage,  the multistage  digester




and further digested to become fine compost.  Microorganisms




functioning in this digester are generally aerobes.  But the




te;nneratm e in the digester rises as digestion proceeds  from




tie upper  stage to the lover stage, uviore the temperature




ranges between 30 C - 60  C.  Accordingly,  the type of  active




r:i rrcorgariisrrs changes as  temperature rises, i.e. from rnesophi-




ILc "--acterifi to tlierrnopr.ilic bacteria.   Multistage digestion




procseds in such o way that the raw coinnost at each  stage is




pilfd 200mm - ^50r,in high.   Sufficient voids are provided




>jO~-.eer. layers for adequate ventilation and the layers themselves




aro gradually txirned over.   This,in turn,  increases  the  voids




v.hich are  moisture evaporation as digestion proceeds.   In




this way,  digestion progresses both repetitively and syner-




t:etically.




     The plant is designed  so that rav,  ccrr.post stays in  the




multistage digester for about three days.




     Ra'.v cou^ost, as discharged frou the rotary drum digester,




is acidic,  but during the  three days in the rraltistage digester,




it changes  froif acidic to  alkali.  Con.post which has undergone




this change is referred to  as "Fresh Conpost".




  \> Maturing Area




     Fresh  CCMII; ost fron the- multistage  digester is transferred




to l!~e next digesting .stage at t'~>e iiiaturing area \\here it i.s




turned into mature rcrnoo.^t.  ?''icrooi'gani&rr.s which are  active




in t-;.o rratur'n/1,  area are  cla = iific-cl as t,hoi-nio|)iii 1 i.c bncterias.




     Ac c-orc' .i n <". ] •>', t!if? ter.'.^t TV) turc of the frivsh conmost ruves




to i? o i o  th^n 7(i> C.  luring dip-pstlon at the maturing  area ,




f;'ori!i corrro'it i.s t>ilod in 1 . ^>m - 2 . Orn high nilcs and air i.s




D::lJcd ffoni the top of tho  -pile towards the bottcn at  a




                           -29-

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controlled  rate by blowers.  The fresh  compost stays at the




raturinf  area for 5 to 7 c'ays , during which it is turned into




nature  compost by air circulation only.   Vinnoving is not




required.




    h-j-2   Environmental Count3measure




   0 Odor Control




     At  the plant, all facilities- other  than the apron conveyor




for refuse  supnly, including the digester,  separator and




transporting- systems, are substantially  closed.   Odors




generated at individual points sro rerioved  by blovers to




miniraize  odor emission.  Odois thus reroved are  passed through




a cor.post filter where odor particles are deposited on porous




mature  compost.   In this way, the odor particles are exposed




to the  respiration and dissolving action of Microorganisms




living vitbin the mature compost.  Additionally, since all




machinery is installed indoors, each area ii satisfactorily




vpntiloted.




   0 Noise  Cortrol




     Because r;ost facilities are indoors, noise  outside the




plant is insignificant.  Therefore, noise control measures




are almost  solely concerned vith protecting operating and




raintenance  personnel against excessive  noise.   Sound-proofing




of noif-.o ^oiircos,  such as r.otois, blowers,  and vibrators,




is done i.hcrover feasible to ir.aintain a  good vcrki.ug environment.




   \) Vibration Control




     The rain souices of vibration at the- plant  are  crushers,




Vilo.vf-rs . and v i I'u'at i ng scrocii^.  Tl'e cruslierri  and \ibrating




.scroors, ho'-ovcr,  are 1 o\\~vj brat Ion types.   l.herover required,




vibration c'aii'~ing systems are used.
                             -30-

-------
   () Control  of Filthy Vater




     Three  basic classes of by-product pollutants  are produced




during plant  operation.




     Class  (A):   Condensate produced during digestion




     Class  (B):   Conpressed by-nroducts from  the rotary drum




                  digester




     Class  (c):   Pollutants released during equipment cleaning-




     Pits are provided at appropriate intervals along aera-




tion and deodorization piping, to collect class(A)pollutants.




Material accumulated  in the pits is Dumped to  the  night soil




sludge treatment plants for ^recessing.




     For both classes (B) and (c) pits are provided  at the




bottom of the rotary  drum digesters.  When material  is accumu-




lates to a  predetermined level,  it is pumped  to the  nipht soil




sledge treatntr t plMit for p: cc ( t-sir^.




    'i-5-3   Heavy 1'eta]  Control




     /s r-yplfiii laid above,  conpoi-t i:-- rlnss-if led as  a  sp;eci£il




f erti li zt-r  by Javan's Miiis tiy of Agriculture  and  Forestry.




Vhich stipulates  that the contents of the three elements shown




in Table 9  must  not exceed certain limits.  For elements shown




in Table 1O,  the  dissolving amounts are regulated.
                             -31-

-------
Table-9  >Ieavy metal  liivits  for  special  f ertilizer( No. 1)




         and analyzed values  for Toyohashi  City conpost




                                                  (Unit;pom)
!Foavy metal
i
'• A.S
. Cd
Kg "
Regulated
value
50 or Less
5 or Less
2 or Less
Toyohashi cocipost
sainole( l)
1.3
1.01
0.68
Toyohashi compos
sample( 2)
1,8
0.99
0.51
t



Table-10  Special fertilizer




          Analysed values for Toyohashi City  compost
' Heavy i/ietal
A'ercury all
-------
     In Toyohashi  City,  toxic refuse which could cause the




presence of heavy  metal  in produced compost is collectd




separately with  the  cooperation of local citizens for




alternative  treatment.




     An Analysis of  heavy  metal presence in the compost pro-




duced at the TOyOjlashi facility (v.hich does not include toxic




material)    vas made.   The results are shown in Tables 9




anc 10.




     After the new plant begins operation,  the analysis




values v:ill  not  exceed the present regulated levels, and




should even  be lower.




     Periodic analysis of  product compost made by the new




plant v/ill to made to assure total safety.
5.  Condlusions




     The LTRECS of Toyohashi  City has  progressed well since the




formation of a project  team  in 1970-   Research concerning on




waste and studies for site location proceeded under the




guidance and with the assistance of the state and prefectural




government authorities  concerned.   Now,  the related agricul-




tural project is rearing  completion.




     This work of the integrated resource recovery and waste




treatment which began in  1970  will be in full operation when




the SHIGENKA Center  is  completed .   At the same time, efforts




vil.l be made to improve  the  overall environment of the co-




mmunity and the state of  local roads.  To do this however means




that various prerequisites must, be mot at an early c'ate.




In t! is connection,  and from tic standpoint of proper
                              -33-

-------
treatment and effective utilization of waste, it is eirphasized




again that concentrated efforts must be made to systematize  se-




paration collection at the collection stage by gaining  the




understanding and cooperation of all local citizens.




     Vhen th^se projects are completed, they should creates




a rr.ore beautiful and natural living environment vith richer




soil, greener trees, cleaner air and fresher water.  Its ulti-




mate success at Toyohashi City should cause similcir systems




to be adopte^ by other communities.




     Those living now should endeavor to create the future




and bequeath the effective utilization of invaluable resources




to the coining generations by converting out thought for the




benefit of profitable utilization of the resources whose exis-




tence is extremely limited.  We firmly believe that this is  a




duty imposed on all of us living today.

-------
                                                                    357
     SOURCE SEPARATION FOR RESOURCE RECOVERY - STATE-OF-THE-ART
                              by
                     Sukehiro Gotoh *
                     Eiji Tanaka    and
                     Yoichi Yonemura
                       November, 1978
* National Institute for Environmental Studies, Tsukuba, Japan
+ Dynax Inc., Tokyo, Japan
# Nomura Research Institute, Kamakura, Japan

-------
                                                                  353
                         ABSTRACT










In the Japanese cities with populations less than 300 000,  recycling or




materials recovery from the refuse is widely practiced through the source




separation assuming some form of citizens' participation.   Very few cities




use a sophisticated mechanized system for resource recovery.  Application




of hand-picking, sorting by screens, or magnetic separation of ferrous




fraction to a source separated waste stream is a common practice for




recycling in many cities.  The state-of-the-art in two cities, one with




a considerable involvement of citizens in the source separation and another




with little, is described in this paper.

-------
                                                                   359





                                                                    1.
BACKGROUND










In Japan, all wastes are classified by law into two categories; the




industrial waste and the general waste.  Current "Waste Disposal and




Public Cleansing Law" defines the industrial waste by names as those




generated from industrial activities and the general waste as the re-




mainder.  Disposal of the general waste is stipulated in the Law as th=




sole responsibility of the local municipality.  The general waste, fro.n




its content, may either be municipal solid waste or nightsoil.  Municiv>a]_




sanitation authorities, however, are becoming more involved in recent




years in the solid waste treatment rather than the nightsoil, since tha




latter is becoming collected by the sewerage.








Historically, source separation of municipal solid waste has been prac .




ticed in a number of ways for the various reasons.  In the post-war




years, there had been essentially no source separation before contains,-_




ization of refuse collection started in many cities for the efficiency




followed by an increase in per-capita generation rate of refuse.  In




those days, all what the residents were asked to do at the source was




to set aside the waste that simply did not fit the designated contair.-i,-




(small bins, steel buckets, paper bags, plastic pales, etc.) and faring




them out to the collection yard at a designated date.  This separated




waste was and is called "bulkies" or bulky waste.








The need for the second type of source separation arose from the fac~




that an increasing number of municipalities had employed incineratirr.

-------
                                                                360
                                                                     2.
 as  the major processing method, partly because of the subsidation of




 this method by the Ministry of Health and Welfare through financing.




 Consequently, all noncombustibles including those materials that are




 considered hazardous or inappropriate-to-burn like chlorinated plastics




 were either encouraged or directed by the municipal authority to separate




 at  the source point.








 For the past few years, particularly since .the oil crisis in late 1973,




 source separation has taken a different direction in Japan.  Resource




 recovery and/or waste reduction has become a primary cause or motivation




 of practicing source separation, in addition to the  causes for an efficient




 collection and proper treatment at the processing plant.
GENERAL STATUS OF SOURCE SEPARATION









On a practical basis, a success or failure of source separation of any




type may largely depend on the citizens' participation.   The degree of




cooperation of residents through actual participation varies from one




city to another, or even one district to another in the  same city depend-




ing on the nature of communities, concerned.  Becuase of  this reason, a




highly urbanized large city is generally reluctant to practice the source




separation, while the authority of a small- or medium-sized, less urbanized




city considers it relatively more feasible in Japan.









Waste Reduction through Recycling






In almost all municipalities where source separation is  now practiced in

-------
                                                                 .361





                                                                      3.
 one way  or another,  at least one  of the  initial motivations of  imple-




 menting  it was to  reduce the amount of waste  that  should be ultimately




 disposed of.   For  this purpose, source separation  may be effective in




 the following  two  ways:  (1)  A portion of potential solid waste  at the




 source  (homes,  offices,  stores, etc.) can be  recycled before it becomes




 waste actually and thus  reduce the  generation of waste.   (2) Separation




 at  the waste "upstream"  can  increase chances  for resource recovery in




 the following  processes  of treatment and thus reduce the amount of waste




 for ultimate disposal.








 The reduction  of potential waste  at the  source is  most desirable for




 a municipal authority.   However,  since the potential waste is not a waste




 yet, the  best  a municipal authority  can  do may be  to suggest and encourage




 the citizens to practice various  means to control  the waste generation.




 Residents' selling newsprint  to secondary materials dealers at home, for




 instance,  is actually  encouraged  by  the  city  and is a. quite common practice




 of  recycling in Japan.   Nevertheless, this sould be an ordinary commercial




 transaction between the  citizen and  the  dealer,' and is beyond the control




 of  the municipality after all.








 Perhaps,  the most popular and widely practiced source separation for re-




 cycling in Japan is the  one often called "group recycling", in which a




 group of people representing a neighborhood club,   ladies association, or




 the  like, cooperate in separating and even  sorting recyclable materials




 at  a point of collection  (yards,   lots,  alleys, etc.)  on a semi-voluntary




basis.   Recyclables so separated may be purchased on-site by a secondary

-------
                                                         362
materials dealer.  However, the revenue gained in this way should not

be refunded to each individual.  Rather it should be returned to the

participated civic groups.



A more systematic source separation for recycling was first invented in

1969 in the Toshima Ward of Tokyo.  In this scheme known today as "the

Toshima method", civic groups, secondary materials dealers and the

Metropolitan Public Cleansing Office of Toshima cooperate each other,

and each plays an important role.  First, the civic groups after having

consulted with secondary materials dealers plan a source separation pro-

gram and announce it to the municipal office.  Then the city according

to the program sends out the city's collection trucks to each yard on

the day to pick up the "left-over" waste that should be transported to

the landfill site.  Since then, many other variations of the Toshima

method, each being different from others in the role of these involved

three parties, have become known.



Resource Recovery from Source-Separated Waste

                                                 *   "    ' '
Since the oil crisis, there" have been a number of municipalities in Japan

which have shown interest in recovering resources out of source-separated

wastes.  Categorization of the refuse at the source changes from one city

to another.  Some employ a three-category collection systems,  and others

even a five-category system.  In Hiroshima, the residents are asked to

separate the waste at the source into five categories; combustibles, non-

combustibles, bulkies, recyclables and hazardous materials.

-------
                                                          363
Often, the noncombustibles and bulkies or the category simply called




"separated waste" or  "resources waste" will be the collected waste




stream that will be chosen by many municipalities to process further for a




materials recovery purpose.  This waste stream normally comprises about




20 percent by weight  of the whole municipal solid waste and should be




landfilled unless otherwise processed (Tokyo Public Cleansing Bureau,




1978).








According to a recent survey made by the Ministry of Health & Welfare,




more than 204 municipalities are currently implementing some kinds of




materials recovery from the collected waste stream.  And more than 38




cities reclaim  secondary materials directly out of a source-separated




fraction called "resources waste".  Ten such cases were studied in detail




by the present authors and their study group and the results are published




in a compiled form (Handbook, 1978).   Also a dozen such source separation/




recycling systems were compactly summarized elsewhere (Gotoh, 1978).  To




illustrate the present situations on the source separation and municipal




recycling, two cases  are selected and reported in the following.
NUMAZU CITY








Facing the Suruga Bay at the foot of the Izu Peninsula, Numazu is one of




the common medium-sized local cities located in the eastern part of




Shizuoka Prefecture of the middle of Honshu.  Since the beginning of 1973,




there has been not much change in populations of the City, being a little

-------
                                                              364
                                                                     6.
more than 200 000.  Unlike the neighboring cities of both Mishima and




Fuji, there are no large-scale industries and plants that are located




in the City.  Only light industries including the processing of marine




products and fisheries are the major industrial activities in Numazu.










City's Solid Waste Management





The City had been burning most of its combustible wastes using an obsolete




batch incinerator, and sending everything else to its sole dumping site




called Kanaoka'District until October, 1973, when the residents nearby




'rose to oppose the continuation of City's sanitation operations because




of its ill management of the dumping site.  This residents' opposition




was so strong that even City's garbage trucks were blocked by the residents




in the area1and as a result the City was forced to stop its waste collection




temporarily.








The Kanaoka conflict was resoluted in January, 1974, by the City's




official agreements with the residents on the terms that the City should




thenceforth take all combustible waste to the incinerator and should look




for other disposal sites at the same time to take off partially the load




to Kanaoka.  Soon after another residents' opposition took place, this time




against the construction of the hewer incineration plant.  Once again this




was resoluted by the City having signed a pact of anti-pollution agree-




ments with the residents of the vicinity.








With all these bitter experiences, the municipal authority had developed




a very unique solid waste management system in which a greater degree of

-------
                                                             365
                                                                     7.
 citizens' participation through source separation was assumed.  The




 system,  initially hinted by a group of City's collection crew members




 and supported by the former Mayor, was aimed primarily to involve as




 many citizens as possible at the collection point and to let them share




 "the garbage problem" together with the City.  In fact, this collection




 system asked the citizen to source-separate the waste into three categories




 and also invited .numerous civic groups to engage in further sorting of




 the separated recyclable waste with the City's collection crew.








 Figure 1  describes diagramatically the present solid waste management




 system in a brief and compact form called Resource Recovery ID Matrix




 (Gotoh & Nakasugi, 1977).  Classification of the waste and some related




 information on the collection is also summarized in Table 1.











 Source Separation and Elaborate Recycling






 The reason that the City's collection crew took the initiative in formu-




 lating this collection system was simple and obvious.   By 1973, the City




 authority was transferring gradually its collection operations to private




 contractors for economic reasons.   Naturally, this was a threat to the




 crew for losing the jobs.  Inspired by the Kanaoka and other incidents,




 leaders of the crew then originated the idea of the present collection




 system and directly proposed it to the Mayor then in a politically dif-




 ficult situation.  It should be noted here that at that time right after




the oil crisis the public concern for recycling was mounted and quite




favorable for this new idea.

-------




















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-------
                                                      367
 In  Numazu,  like many other cities, wastes should be separated at the




 source broadly into three kinds; combustibles, landfillables and re-




 cyclables.   Combustibles go to the new 300 TPD incinerator equipped




 with modern pollution abatement measures which was built and went into




 operation in late  1976.  Landfillables, mostly noncombustibles and




 inappropriates-for-burning in its content, are collected and directly




 hauled to the newly aquired disposal site in the coastal swamp area.




 Recyclables so separated at the source include essentially metal cans




 and glass bottles.








 It  is this  recyclable waste that the City authority decided to ask the




 citizens to cooperate for an elaborate sorting before it should be col-




 lected by the City.  Utilizing  the organizational function of traditional




 civic groups  such as block associations,  the City first had designated




 about 500 open spaces on the roadside, by the public building, or in the




park, as the  collection station for the recyclables and landfillables




within the  municipal area.  It is important to note that these selected




spaces are  used only for the day and the night before the collection that




comes once  every month. The spaces are not allowed to be used for this




purpose on  other days.   This means that the citizens keep those materials




at  their home for about a month.   On the  collection day each civic group




selects and sends "caretakers", on a voluntary basis but actually in turn,




to  the station so as to engage in caretaking other people.   The caretakers




sort the recyclables out and help the City collection crew pick up the




naterials and the waste at the station.

-------
                                                            368
                                                                     10.
The way that the recyclables are brought to the station and sorted out




by the citizens, and collected by the City crew is sketched in Figures 2




S 3, respectively.  Note here that the caretakers not only help separate




wastes coarsely by rearranging but also even take caps and ir.etal tips




off the bottles to increase the product value.  The reason that in Numazu,




unlike other cities, very little newsprint and other paper stock is re-




cycled in this way may be explained by the fact that the neighboring




Fuji City is known for its large paper mills and a number of private




waste paper collectors buy out these materials before they are brought




to the recycling station by the citizens.








Before this elaborate recycling scheme, known today widely as "the Numazu




method", was implemented, the City authority had planned carefully its




operational program.  Mobilizing almost all collection crew members of




the Sanitation Department, the City made an allout effort in public




relations; groups of crew members had visited every one of civic assoc-




iations to be involved and explained the need for waste reduction through




recycling and proper disposal through source separation.  They also pro-




mised that in reward for the cooperative service at the station a portion




of revenues gained by recycling should be returned to each civic group.




Collection crew members were electe^ for this public relations job because




they were the people who meet the citizens regularly.  Also the City had




experimented this method in a selected model district before the system




was formally applied to the whole City area.

-------
                                                            369
                                                                    11.
Effects of Resource Recovery





Of the collected recyclables, "live" bottles and glass cullet are directly




sold to secondary materials dealers by the City as a broker.   ("Live"




bottles mean those glass bottles with a standard size and shape like most




Sake and beer bottles.)  Metal cans are collected in wire-meshed square




baskets and truck-hauled to the City's work yard next-to the  incineration




plant.  There a further sorting into steel (tin)  cans .and aluminum ones




by the magnet separator and hand removal of contaminants are  performed




by the City employees.  Metal cans are pressed to a block before they




are sold.  The operation at the work yard is pictorially given in Figure 4.








The effect of recycling on reducing the amount of waste to be landfilled




may be measured by the following figures.  For the period of  six months




starting from April, 1974, the City filled  3 597 tons* of mostly non-




combustible wastes.  For the same six months period in the following year




when the City had implememted the present source separation program for




recycling, only  2 814 tons of wastes had been landfilled. Assuming that




there was no significant increase in total amount of waste generated,




22 percent of waste reduction was achieved by this source separation/




recycling  program.








Table 2 indicates tons of glass and metals that had been actually recycled




and amounts of the revenues that had been returned to the participated










*  Throughout this paper, all tons are metric tons (One ton = 1 000 kg).

-------
                                                                                                                     370
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-------
                                                              371
                                                                     13.
civic groups and gained by the City Treasurer, for the first eight




months of the program in 1975.  Amounts of metal scraps that had been




recycled in the fiscal 1976 and partly in 1977 are listed for each month




in Table 3.  (The Japanese fiscal year starts from April 1st.)
FUCHU CITY










Fuchu is one of the typical suburban cities which is located on the




western periphery of the Special Districts of Metropolis Tokyo.  As of




March, 1978, the population of the City is ca. 187 ,000, being almost




more than doubled since the early 1960*s.  This urbanization is charac-




terized by a steady increase of the residential area and also the related




areas of transportation, commerce and recreation.  Like other satellite




cities, a large fraction of residents are commuters to Tokyo.










Solid Waste Management





The City, like other neighboring ones, collects its general waste by




providing each station with a pair of large steel containers called




specifically "Dust-box", one painted in green and another colored in




orange.  The green container accepts combustibles while the orange one




noncombustibles.  Bulky wastes are collected only upon the request of




citizens.  Fuchu has employed this collection system since 1966,  which




is not necessarily a common method of collection in Japan, because a




large container placed along alleys and streets often causes traffic




problems and some difficulty in collection.  In fact, in areas of highly




crowded downtown district of the City, these containers are not used.

-------
                                                                372
                                                                    14.
Table  3    Metal  Scraps  Separated and Recycled  (Numazu  City)

                                                   (All fig-res- in tons-)
Month
April
May
June
July
August
September
October
November
December
January
February
March
Total
Steel
FY1976
23
27
22
28
40
39
31
24
23
16
16
19
308
cans
FY1977
30
32
43
49 »
48
48
49
40
40
—
—
—
379
Other
ferrous
FY1976
12
13
14
15
15
17
14
16
26
10
9
16
177
scraps
FY1977
25
33
24
27
18
22
21
19
33
--
—
—
222
Aluminum cans
FY1977
—
—
—
—
2.3*
2.2
1.9
1.3
1.5
—
—
—
9.2
   *  Aluminum separation  was started from August,  1977, for the first time.

 N.B. Glass bottles were recycled at the same time whose revenue should be
      returned to participated civic groups.  They are  counted in numbers.
      However, estimated weights for fiscal 1976 and 1977 are 1 710 and 1 522
      tons, respectively.

-------
                                                             373
                                                                    15.
After collection, the noncombustibles and bulkies should be transported



to a treatment plant that the City owns but is operated by a private



contractor.  There the wastes are processed to "skim off" the recyclables



and the residue is hauled out to be landfilled.  On the  other hand, the
                          uejtii
combustibles collected threertimes a week are hauled to an incineration
                            N


plant that is owned jointly by the City with other two neighboring cities,



Chofu and Koganei..  The incinerator is operated by a unionized public



authority known as the Nimaibashi Sanitation Union.  The incineration



residue is dumped at a small landfill site in Fuchu.






An overall solid waste management scheme of the City is described in the



diagram of Figure 5.  Also amounts of solid wastes the City had collected



and accepted at the incinerator for the past five fiscal years are shown



in Table 4.








Source Separation and Resource Recovery




Originally the source separation using a pair of larga containers was



initiated in order to increase the operational efficiency of City's



solid waste management system.   Collection operations by using these



containers could be highly mechanized and thus saved labor costs a lot.



Also source separation of the noncombustibles had reduced the load to



the jointly owned incinerator,  simply because these wastes had been directly



sent to the landfill site.  The residents did not feel much inconvenience



in only separating the waste into two categories at the source.  Rather



they found it very convenient to be able to discard the waste whenever



they wanted,  instead of carrying and placing the wastes at a designated

-------
374
     16.
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-------
                                                            375
                                                                    17.
time.  This type of source separation has now become a part of City's




solid waste management system and has contributed to the efficiency and




the proper treatment of the solid waste.  In this case, the source sepa-




ration is not directly related to the resource recovery.








Like other suburban cities located in the Tokyo Prefecture, Fuchu started




considering resource recovery around 1974 as a basic means for reducing




the ultimate waste.  This was motivated by an incident,  since about 1965,




many gravel pits in the upper Tama River District near the Town of Mizuho




had become the disposal sites of both industrial and municipal wastes




from these cities until 1973, when the citizens of Mizuho and of the




vicinity filed a lawsuit because of the damage due to secondary pollutions




and environmental destruction caused by the waste disposal.  Fuchu was




one of the municipalities that had dumped the nonconvbustibles and incin-




erator residue in the area for years.  .The incident called "Another War




against Waste" was terminated in 1976 by a court decision that the area




should be no longer the garbage disposal site.








Because of this incident, the City had to construct a treatment plant of




its own for the noncombustibles and bulkies in late 1975 to reduce the




amount of collected wastes through recycling.  For the purpose of pro-




cessing mainly the noncombustible waste whose collection fron the con-




tainer by the truck is depicted in Figure 6,  the plant started its oper-




ation from April, 1976.  A general overview of the plant is shown in




Figure 7, where the wastes are sorted and hand-picked mostly from the




conveyors each connected in sequence.  Other than the conveyors, only




mechanized portions are the magnetic separator for ferrous fraction

-------
                                                          370
                                                                    18.
recovery and the subsequent press that is operated hydraulically.  The




outputs of the plant are ferrous scraps, hand-picked bottles,  glass




cullet, and non-ferrous (aluminum)  metals for recycling,  and plastics,




woods and dirts for ultimate disposal.










Operation of Resource Recovery Plant





The plant itself was built and owned by the City.   However, it has been




operated by a private contractor since the beginning.  This was the




City's policy-'








Since the contract should be renewed every fiscal  year by an open bidding,




the contractor may change from one  year to another.  And  actually the




contractor who won the contract  of the first FY 1976 did not succeed




in the following year.








The method of operating this resource recovery plant which is  specified




in the detailed contractual agreements to be exchanged between the City




and the firm may be summarized as follows:




(1) The contractor through operation of the facilities agrees to recover




    as much recyclables as possible.  (No minimum  amount  or ratio of re-




    covery is specified, however.)




(2) The City pays the cost of all utilities (water, electricity, etc.)




    that are consumed to operate the plant.




(3) The City pays to the contractor an agreed amount of contractual fee




    on a monthly basis for the period of contract.

-------
                                                                 377
                                                                    19.
 (4) The work hours of a weekday are agreed from 8:30 to 17:30, with a




    maximum two hour extension per day permissible for which the City




    agrees to pay 10,000 yens per hour.




 (5) All the revenues obtained by selling the recycled materials belong




    to the City Treasury.  However, if this sales revenue exceeds the




    contractual fee the City pays to the contractor, 20-.percent of the




    excess amount should be refunded to the contractor as an incentive




    payment.




 (6) All the recovered materials at the plant should be sold by the City




    itself in a competitive bid.  The contracted operator of the plant




    is not allowed to become a bidder.








After two years of operation by different contractors in each fiscal




year,- the City has obtained the following results from this resource




recovery plant.  See Table 5.  Here note that in the second year of




operation (FY 1977} nearly twice as much recycling was achieved as




compared with the first year although the averaged unit price of most




secondary materials had not much changed.  It appears from this that the




more valuables were recycled selectively.











Net Operating Cost of the Plant






From the operation of the resource recovery plant for processing non-




combustible and bulky wastes, the net operating cost per ton of incoming




waste for the fiscal 1977 can be calculated as low as 1,130 yens (3.77*










*  Currency exchange rate of 1 US dollar = 300 yens is assured in all case:

-------
                                                                                                               378
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-------
                                                             379





                                                                    21.
US dollars).  See Table 6 for details.  Cost reduction due to the




revenues from recycled materials is indeed noteworthy.







This net operating cost per ton should be compared with other processing




costs in order to identify the effect of recycling.  For the same fiscal




year, the City reports the following processing costs per ton of the




refuse; 5,537 yens/ton for incinerating the combustible waste and




3,470 yens/ton for landfilling the remaining waste (Handbook, 1978).




These per ton costs do not include the collection and transportation cost,




and can be considered the net costs associated with operations at the




incineration plant and landfill site,  respectively.  Since the present




resource recovery plant is for processing the noncombustibles and bulkies,




the net operating cost of 1,130 yens/ton can be directly comparable  with




that of landfilling which is another alternative. It may be concluded




therefore that the City,  by taking this recycling alternative for the




noncombustibles and bulkies,  saves 2,360 yens ( 7.87 US dollars)  for each




ton of the wastes collected.
CONCLUSIONS







Emphasis is placed in this paper on the recent efforts for resource re-




covery made by the Japanese municipalities utilizing source-separated




wastes.  It has been shown that in small or medium-sized cities the




source separation by the citizens tends to be programed for the purpose




of resource recovery since the oil  crisis in 1973.  In particular, those

-------
                                                            380
                                                                   22.
Table 6     The Net Operating  Cost in FY 1977 (Fuchu City)
Cost/Revenue
Items
1. Contractual Fee
2. Salary*
3. Incentive Payment**
Total Cost
4. Sales of the Recycled?;
(l.)-f(2.)+(3.)-(4.)
Direct Cost,
in
thousand yens
30,360
4,500
1,420
36,280
27,099
9,181
Cost/Revenue
in
yens /ton



4,467
3,336
1,130
       * A City personnel is dispatched to the  plant as the supervisor.
      ** (27,099 - 20,000) X 0.20 = 1,420 thousand yens.
       i? See Table 5-  Also from this,  8 122  tons of waste is assumed to
         have been processed at the plant.
                     01. >
    Source:  Public Cleaning Section, Division of Environment, Fuchu City,
            August, 1978.

-------
                                                       381
                                                                    23.
municipalities with some difficulties  in obtaining the landfill disposal




site are very anxious about the recycling alternative.








Two cities, Numazu and Fuchu where such source separation/recycling




programs are being implemented have been taken as the cases for study




to show the present Japanese situation.  It has been demonstrated that,




in the Nuraazu case, citizens' involvement in the source separation is




quite extensive and actually effective for the following recycling




operations by the City, and, in Fuchu, by running a resource recovery




plant the City can achieve a substantial cost reduction in processing




the noncombustibles and bulkies that are separated at the source.








Finally, it should be pointed out that, in Japan, the source-separated




wastes could be an ample and practical input to a recycling plant  run




by the municipality.

-------
                                                                382
                                                                   24.
                 REFERENCES CITED
Waste Recycling Study Group, 1978.  Recycling Handbook.  Haikibutsu
          Shigenka Kenkyukai, Tokyo, ca. 300 pages. (In Japanese)

Gotoh, S., 1978. "Summary of Waste Management Operations by the Resource
          Recovery Identification Matrix", in Study on Evaluation of Re-
          source Recovery Technology Systems, pp 247 - 253, Annual Report
          to AIST. (Contract Research).  Japan Industrial Technology Pro-
          motion Association, Tokyo.  (In Japanese)

Gotoh, S. Gt O. Nakasugi, 1977. "An Economical Evaluation on Urban Waste
          Resource Recovery Systems", IFAC Symposium on .Environmental
          Systems, August 1-5, 1977. Kyoto.  (In English)

Public Cleansing Bureau, 1978.  Annual Report of FY 1978.  Tokyo Metro-
          politan Government, Tokyo. 158 pages. (In Japanese)

Nomura Research Institute, 1978.  Survey Report on the Waste Reutilization.
          Contract Research (FY 1977) of Division of Water Supply &
          Environment, Ministry of Health £ Welfare, Tokyo. 160 pages.
          (In Japanese)

-------
                                                                383
                        LIST OF FIGURES



Figure 1    Waste Flow and Operation Diagram  (Nuinazu City)


Figure 2    Sorting of Recyclables by Caretakers  in Nuinazu


Figure 3    Collection of Source Separated Materials at A Station
            in Nuinazu


Figure 4    Separation of Aluminum Cans from  Steel Cans at the
            Numazu Work Yard


Figure 5    Waste Flow and Operation Diagram  (Fuchu City)


Figure 6    Collection of Noncombustibles from the Container
            in Fuchu


Figure 7    A View of Fuchu's Resource Recovery Plant
                                                                     25.

-------
                                                         384
^N. Involvement
Location ^\.
& Operations ^\.
SOURCE

TRANSFER
STATION

PROCESSING
FACILITY
DISPOSAL
SITE
Generation
Separation
/Sorting
Collection
Separation
/Sorting
Transport
Sorting
Shredding
Separation
/Sorting
Conversion
/Incineration
Energy /Matrl.
Recovery
Residuals
Treatment
Sorting
Shredding
/Sorting
Landf illing
/Managemnt.
Landf ormation
/Reclamation
Land Use
Citizen
.Q.OO
L L ia
Municipality
/Public Authority

32
y V '^i
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d
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/Resources Dealer





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— ^0 ©
Waste S





Secondary Materl.
/Energy/Land
User










treams
11: Combustibles
21: Landf illables
31: Recyclables
(glass, metals)
11~13: ca
op
CO
. 60% of .
eration by
ntractors.
Legend:
                                        Direction of Materials/Energy Flow
                                        Waste Generation £ Termination
                                        Operations Executed
Figure   1    Waste Flow and Operation Diagram  (Numazu  City)

-------
                                                               385
Figure 2
     1 :  Caretakers




     2 :  "Live" Bottles Separated




     3 :  Five-gallon Metal Containers for Glass Gullet




     4 :  Wire-meshed Baskets for Cans




     5 :  Citizens Carrying Recyclables to the Station

-------
386
           o
          O

-------
                                                         387
Figure 3
    1 : Rice Sack (Before)




    2 : Plastic Basket (Now)




    3 : Cans in Wire-meshed Baskets




    4 : Glass Gullet in Five-galIon Cans




    6 : Collection Truck for Cans




    7 : Collection Truck for Bottles

-------
388
                m
                 .j
                 r"
                 i

-------
                                                                       389
Figure
    1   Receiving Conveyor




    2   Magnetic Separator




    3   Steel Cans Separated




    4   Aluminum Cans Recovered




    5   Hand-picked Rejects




    6   Hydraulic Press

-------
39O
           o
           O"
            i
           ' r

-------
                                                            391
^v. Involvement
Location ^x.
& Operations ^\^^
SOURCE

TRANSFER
STATION

PROCESSING
FACILITY
DISPOSAL
SITE
Generation.
Separation
/Sorting
Collection
Separation
/Sorting
Transport
Sorting
Shredding
Separation
/Sorting
Conversion
/Incineration
Energy /Matrl.
Recovery
Residuals
Treatment
Sorting
Shredding
/Sorting
Landf illing
/ManaReinnt.
Landf ornat ion
/Reclamation
Land Use
Citizen
.^00
Municipality
/Public Authority

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Secondary Materl.
/Resources Dealer
Secondary Materl.
/Energy/Land
User
i
Waste Streams
11: Combustibles
21: Sulkies
31: Noncombustibles ,


32~33: Contracted
operations.
24 ~ 37 :~\
-, _ ° > Contracted
34 ~ 37: J
J operations.
'•^ 14-15: Done at
	 j jointly owned
• incinerator.
i
f

'36
f
137


L




81
	 >®















Legend:
                                        Direction of Materials/Energy Flov
                                        Waste Generation &  Termination
                                        Operations Executed
Figure   5    Waste Flow  and Operation Diagram (Fuchu  City)

-------
                                                                392
Figure 6
    1 : Green Colored Container for Combustible Waste




    2 : Orange Colored Steel Container for Noncombustibles




    3 : Collection Truck with A Crane

-------
393

-------
                                                                  394
Figure 7









    1 :  Unloading Hopper




    2 :  Magnetic Separator




    3 :  No. 1 Belt Conveyor




    4 :  No. 2 Belt Conveyor




    5 :  No. 3 Belt Conveyor




    6 :  No. 4 Belt Conveyor




    7 :  No. 5'Belt Conveyor




    8 :  No. 6 Belt Conveyor




    9 :  No. 7 Belt Conveyor




   10 :  Hydraulic Press




   11 :  Compressed Ferrous Scraps for Recovery




   12 :  Glass Gullet (Flint)  for Recovery




   13 :  Glass Cullet (Color)  for Recovery




   14 :  Plastics and Others for Disposal




   15 :  Floors for Hand-picked Materials




   16 :  Receiving Floor for Bulky Items

-------
                                                             395
CO,
 in   CM'

-------
                                                        396

ORGANISATION FOR ECONOMIC        RESTR_ICT_ED

                                 Paris, 16th October, 197S
CO-OPERATION AND DEVELOPMENT
  Environment Directorate          .To:   Delegates  to the V.'aste
       	-~—                    Management Policy Group
        ENV/WMP/78.5
                                   /Copy to  National Delegations/
          Scale  D
                                                        Or.  Eng.
                   EITVIROEHEl'T. COIMITTEE



                WASTE, MNAGEMENT POLICY,.GROUP



                          Case Study


                    Economic Incentives for

       'Municipal V/aste Collection and Recovery  in  Japan
       This paper, prepared by the Secretariat  reviews  a  number
of schemes and economic incentives for the  collection and
recovery of municipal waste, adopted in various municipalities
in Japan.


ACTION REQUIRED:  For discussion.
42608

-------
                                                    Eirv/¥MP/78.:
                                  JF_OR
            WASTE CpjLIECTJOIf AjH), REjyjERJ_ III jTAPAIT


IlITRODDCTIpir

                  t_o_' _the_ Probl_ems
       The final disposal  of municipal waste  is  dealt with in
Japan as in most OSCI) Member countries,  either in  the fom. of
landfill or incineration,  and landfill is  the final  step in all
waste treatment (1 ).

       According to J. "ilcox (1977) landfill is the cheapest
method of waste disposal,  ai least in the  United States  and the
United ICingdoin(2).  However, as he noted,  there  are  drawbacks
in landfills, even in the  case of sanitary or controlled land-
fills(3).  First, landfill- of untreated  waste does preclude
recycling;  second, it also precludes the  use of waste for
energy generation.

       In addition to the  above-mentioned  drawbacks,  there are
two distinct circumstances in Japan which  made landfill  treat-
ment difficult and expensive and consequently prompted Japanese
municipal authorities" to take some measures to reduce the
generation of waste.  These are:  (i) shortage of landfill
sites and the high cost in obtaining new ones;   (ii)  stringent
environmental regulations  imposed on incineration facilities
and landfill sites.
(1) In Tokyo, for example, generation of solid waste was  47  tons/
    miles2 per day in 1975.  Tolcyo Metropolitan G-ovemment is
    responsible for the management of domestic waste.  47 per
    cent of domestic waste was incinerated, 34 per cent of which
    was for landfill and 2 per cent composted and another 17 per
    cent was out of municipal activities.  (Eiji Tanaka,  .Brief.
(2) Wilcox, J. 1977.  Municipal V/aste:  Economic Aspects  of
    Technological Alternatives in Resoiirce Conservation,  Social
    and Economic Dimensions of Recycling, ed. by D.I/. Pearce
    and I. Walter, ITew York University Press, 1377.

(3) In cases where land reclamation is carried out by irregular
    methods or without sufficient pretreatnert of the wastes
    in question, undesirable results may occur such as the con-
    tamination of ground water from landfill seepage or the
    emanation of noxious odours from gases produced by anaerobi
    decomposition.  Without proper supervision such landfills
    may even become breeding grounds for nice and insect  pesto.

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                                                               398

 EI1V/WMP/78.5
       Numerous cases have been reported where municipal  authori
ties faced  strong opposition from residents living near the
planned landfill sites" or construction sites  of incineration
facilities  on the grounds that landfill sites or incineration
facilities  cause pollution(1 ) .

       In order to cope with these crisis situations, .several
municipal authorities adopted schemes to reduce the amount of
waste to be disposed of by reclaiming recoverable waste in
co-operation with commercial recycling dealers and citizens.
       The schemes which these municipal authorities are 'encourag-
ing or adopting can be summarised as follows:

(1)    Municipal authorities subsidize commercial recycling
       dealers (Ueda city).

(2)    Municipal authorities make contracts with private recycl-
       ing dealers- for the treatment of recoverable waste
       (Fuchu city) .

(3)    Municipal authorities install processing facilities and
       lend them to dealers for free or nearly free of charge
       (Shiki city).

(4)    Municipal authorities purchase recoverable wastes from
       citizens and deliver them to commercial recycling dealers
       (Hiratsulca city).

(5)    Recycling activities by a private firm without any
       financial help from municipal authorities.

(6)    Reclamation of waste within the framework of a municipal
       waste disposal system but by mobilising voluntary
       activity of citizen groups or initiative by public field
       wor leers .

       First of all we should keep in mind that these resource
recovery measures have been initiated in response to crisis
situations, rather than cost saving possibilities for municipal
expenditure of waste treatment.  However, we can certainly see


(1) We see similar c?see reported in California, United States.
    (The Privatisation of Public Services:  Solid Waste ar.d
    Waste Water Disposal EIIV/URB-U3/73. 104 C'j?/U?J3/7l6).  It says
    "Today, residents of non-urban areas commonly refuse to let
    their communities host a city clump or sanitary landfill for
    'City Folks' »„.   New landfill sites are difficult to find.
    \/hen they are found, the public protests, and the sites can-
    not be used;   or the site is too remote and hauling waste
    is too expensive;  or the landfills are too sinall to get the
    ecoromies of scale needed to keep costs down to some
    reasonable level."

-------
                               -  5  -                 ENV/WEP/78.5
 that  in  the above  schemes,  intentionally  or  unintentionally
 economic mechanisms  are working  and municipal  authorities  are
 acting in  order  to minimise  total municipal  expenditure  for
 waste management by  using incentives -to commercial  dealers and
 citizens.

       Many local  authorities intend to consign  recycling  to com-
 mercial  dealers  because commercial scrap  dealers often have
 better expertise in  resource recovery.  They employ skilled but
 not expensive labour and they have efficient processing  systems,
 which result in  lower processing costs and higher reduction of
 waste.   Commercial dealers would not, of  course,  participate
 in recycling schemes without reasonable profit.   Therefore, it
 is sometimes necessary for municipal authorities  to provide cer-
 tain economic incentives to dealers.

       Let us look at this from  a more theoretical  point of view.

       In Japan, as  in most other countries, most consumers have
 free use of municipal waste collection services(l).

       This creates  a divergence between  private  costs of  waste
 disposal, which  are  zero, and social costs of  waste  disposal,
 most of  which are  reflected in municipal  btidgets  for waste
 collection, incineration, landfill, and the  like.   Simply
 charging consumers for the full  social costs of  disposal would
 correct  the market failure and create new incentives for reducing
 the amount of waste  and turning  their recoverable waste  to  scrap
 dealers.  However, this charge system has one  important  drawback;
 this could provide an incentive  for increased  littering  and accu-
mulation of waste.   Because littering involves larger social
 costs and accxunulation of waste may cause sanitary  problems,
 careful  consideration would be necessary  before applying this
 charge system(2).

       Subsidies for recyclers,  in principle,  also  correct  the
 source of market failure attributable to  free  disposal by
households.  A Japanese case study, which is extracted from
 Japanese municipal experiences,  can be thought of basically as
(1) Of course, waste collection service users and other people
    pay for the service through local taxes and even national
    taxes at times, if the central government subsidises local
    finances.  "?re_e use of municipal waste collection service"
    here means th"a~t there is no direct relationship between the
    cost of the service rendered to each user and the tax which
    that user pays, i.e. zero marginal cost pricing.  (See
    Financing of Municipal Services Collecting Household and
    Allied Types of Waste - El,rY/URB7US/77.07 CT/URB/707).

(2) See Quigley, Keeper.  The Economicc of Refuse pollec_tij3r
    Ballinger Publishing ConpanVV "CVnYricfg'e," IfaVsY VSTC","" pY'97.

-------
                                                           400

3ITV/WMP/78.5                  -  4  -
subsidies by municipal authorities -for recyclers  or  recycling
activities.  .The maximum subsidy which could  be -justified on
efficiency grounds would eqiial the full  social costs 'of  post-
consumer waste disposal saved by recycling.

5 •     l!he_ .alms. _of the ischem_e-s__and their j>rajrbical_ jneans

       The schemes 'that have been introduced  vary from municipa-
lity to municipality.  However, they seem to  have common aims,
i.e. to save municipal expenditures for  waste disposal by reduc-
ing the amount of waste in order to cope with the shortage of
landfill sites and also prolong the life of landfills.

       In carrying out these schemes, segregation of waste at
source and encouraging participation between  the  public,  industry
and citizens have played very important  roles and contributed a
lot to increased awareness of greater re-use, recycling  and
reclamation of waste.

       ,Let us describe briefly how segregation at source  and
 fublic participation are actually done in Japanese municipalities.
 The following is the abstract from .Brief Report fo.fr_.S.o.urcje
          JLn.T Aa^.aS * EiOi Tanalca, June 1   ~
       In Japan domestic wastes are usually discharged either  in
the form of mixed wastes or separated into two - combustible and
non-combtistible wastes.  This discharge method is not appropriate
for resource recovery because it requires a large amount  of
labour and expensive equipment to extract material from waste,
Therefore, some Japanese local authorities have started new
source separation systems.

       Such local authorities usually reqxiest residents to
separate wastes into three categories at discharge, namely, com-
bustible, n oii-conibustible and "resource" wastes.  "Resource
wastes" include papers, metals, glass etc. which are reclaimable.

 :      In addition  to  the above-mentioned local authority ir.i-
tiated source  separation schemes, there are  other recycling
routes which are voluntary.  Voluntary recycling includes group
recycling and' individual recycling.   Group recycling  activities
depend on such community organisations as children's  circles,
Women's associations,  senior citizens' groups  and residents'
associations.  Revenue  from scrap sales usually belongs  to the
organisations.  Individual recycling  is conducted by  "waste goods"
dealers who collect the different waste materials  (i.e.  nev/s-
papers, magazines,  returnable bottles, inetalv/orlc) from residential
areas.  These  materials are bought  for cash  or in exchange fpr
such goods as  paper tissues.  Local authorities appreciate volun-
tary recycling since solid waste can  be reduced by  these voluntary
recycling activities with little or no assistance by  then.

       Table I gives a  summery  of separation at  source,  collection
and sorting of municipal wastes in  Japan.

       In the  next  Chapter, we  will see  the  experiences  of the
Japanese municipalities according to  the  categories of schemes
they have introduced.   Categories 1 to 4  will be mainly
discussed.

-------
                                 -  5  -
           4O1



ENV/W/78.5


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-------
                                                              402

 ENV/WMP/78.5                 - 6 -



 II .     MUNICIPAL. JXPEjlIEi;CE.S( 1 )

 1 •      Subsidy.. _tp_ JPACZC l_ing
        Prom  the  viewpoint  of the municipality,  recycling activi-
 ties by commercial  dealers are  at  the  same  time a saving of waste
 disposal in  relation  to  the amount recycled.   In this sense,
 the" municipal authority  would be willing to pay for a recycling
 dealer  part  of the  fee (dumping fee) within the amount which it
 would have cost  the municipal authority if  they had carried out
 the waste disposal  by themselves.   For a recycling dealer,  the
 dumping fee  paid by the  municipal  authority contributes to  the
 compensation for the  deficit that  he may otherwise suffer and
 at the  same  time would act as an incentive  for resource recovery.
 Cases exist  in Japan  where municipal authorities contracted out
 part of their waste treatment activities, especially reclaiming
 waste activities to commercial  dealers.   We will see Ueda city
 as an example.

 UEDA PITY (Nagano Prefecture.! Population 105,125 - 1975

        (i) Background

        Recycling of domestic waste in  Ueda  city v/as stimulated
 by the  shortage  of  landfill sites  and  has been practised since
 1966 by the  initiative of  a  private recycling  company.   This
 company proposed to the  city authority that by reclaiming
 recoverable  waste,  they  could reduce the amount of waste to a
 greater degree.  However,  at that  time,  city authorities did
 not give  any help to  the recyclers.

        The results  obtained within the first few years showed
 a definite reduction  in  the amount of  waste to be filled, which
 led the  city authorities to recognise  the capability of the com-
 pany and  to  make contracts with the company for handling re-
 coverable waste.

        (ii)  Municipal waste treatment  in Ueda  city

        The amount of  waste collected in Ueda city is shown  in
 Pig. I.

        The flow  chart of municipal waste management is shown in
 Pig. II.  In Ueda city, municipal  waste  is  collected separately
 according to combustible and non-combustible waste.  80 per cent
 of collection is carried out by city authorities and the rest
 (mainly non-combustible waste)  is  collected by a private company
which has made a contract  with  the city authorities.  (This
 collection company  is different from the company which deals in
 reclamation  of waste).   The  non-combustible waste collected is
 transported  to the  stockyard of the recycling  company, and  then
 urocessed through the belt-conveyor system  with both manual
 and magnetic separation  at the  factory,  which  is managed by the
 company.  This processing  scheme is shown in Figure III.


 (1)  The fcilc-yir.g data and  description are  meetly based on
    £ii^--"ika Hand"!-; or1- (H_avc|'boo_l: _..f o.r Fte source, Recover:';') .
    Hr1T:Y'3v7t~:-:v~ Sl^'^-J-Lca" liVnTryukai  (Study Group  for" the Resource
    Rcc every frcn Waste).   Tokyo,  March  1978.

-------
       - 7 -
                                       403
                                                           ENV/WMP/78.5
FIGURE  1
An
IXXI
Hit

10!
11. 1

lount of Waste
ton
The amount of w
collected
1 	 1M259






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4-
                              4 - Combustible
                              1     Waste
FY 1966  67    68   69    70    71   72    73
                            75
                              -v	Non-conitustible
                                     Waste

-------
     ENV/WMP/78.5
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                                                                    405
                                      - 9  -
                                                            EFV/WMP/78.5
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-------
                                                             406


 EIJV/WI-IP/78.5                 - 10 -
        (iii) Contract between city authority and recycling com-
             pany with, respect to resource recovery

        In the scheme employed by Ueda city, the private company
dealing with resource recovery plays an essential role.   Ori-
ginally this company initiated resource recovery and later on
Ueda city authorities made a contract with the company, realising
that the role played by the firm contributed a lot in reducing
the amount of waste and considering it necessary to integrate
its activities into the municipal waste collection system.

        It is thus in our interest to see the contents of  the con-
tract between city authorities and the company.  The main points
of the  contract are:

(a)     The company sorts and reclaims waste which has been
        collected and transported to its stockyard.  Waste which
        the company finds impossible to reclaim will be trans-
        ported and disposed of by them at a place designated by
        the Ueda city authorities.  Concerning plastic material,
        the company will be responsible for crushing it and the
        city authorities will take the responsibility of trans-
       portation and disposal.

(b)    Ueda city pays the company 556,000 yen per month ($2,780).
        (H.B.  V/e used 01  = 200 yen) for reclamation and
        75,000 yen (C375)  per month for crushing residual waste
       for landfill (in 1976).

(c)    The term of the contract is one year.

(d)    Ueda city reserves the right to investigate the company's
       facilities and may aslc it to submit reports v/henever the
       city authorities deem necessary.

       (iv)  Costs and effects of resource recovery

(a)    Estimated amount of recovered non-combustible waste
       (in weight)

                            Table II
' Landfill
i
i
• — -••» .....
| Recovered
! material

Plastics
Sand and Soil


Ferrous metals
Glass and bottles
Others
25 2&,'>}
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. .

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^ I /
27



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	 t

-------
                     407

                  EiTV/hT-a>/7G.5
("b)  One of the main issues in this scheme is the profitability
   of the private company which deals with recycling because
   viability of this scheme heavily depends on this point.

   Table III shows Estimated Sales Revenue and Table IV
   Estimated Costs for Resource Recovery (according to an
   estimate by Ueda city from the 1975 business account of
   the company). Estimated costs for resource recovery
   exceeds"estimated sales revenue by 3,833,000 yen
   (319,165).

          Table III
     I     Estimation of sales revenue(2)
     iRecovered
     !-•	..-	 - — ._....
                  Estimated Unif
     i,-con;i,i;  ?        « Sales Price I
Ferrous metalsf  560
     k
          ¥5,600,000 (G26,000)r ¥10,000/ton

Glass &    1,740
          ii
           5,220,000 (826,100)' 3,000/ton
jbottles (535°) f
[others (2#) |  66  I 660,000 (S3, 300) \ 10,000/ton {
[(paper, non- I     \        r     ?
(ferrous metals)     f        \     :

|  Total ~T~2»366  [ 11,480,000 (057,400)*     j
(1) Calculated from the amount of nor.-combuctible \vaste in 1975,
 i.e. 3,286t.

(2) This is calculated by assuming estimated unit sales price.


         TableET
f Item
g, 	 	 	 ,._.., __ . , 	 	
f ' "* """"^ TT
| Labour
| Utilities, fuels
t
I Depreciation
r
t Interest
••Jt-^-*. 41 	 •.
»

»
>
»
;
k
f
«
f
Yen
.M A-*. ^. _•. ---..— . 	 — 	 - IT t

11,760,000
1,200,000
1,742,000

611,000
uf


(58,800)
( 6,000)
( 8,710)

( 3,055)
' I
—4
>
I
n
?
t
I

i
   [ Total     [ 15,313,000  (75,565) |


   Ueda city paid the following amount of money to the
Company (see Table V).

-------
EIT7/WMP/78.5
- 12 -
                                                              408
                           Table V
                                         In  thousand  Yen
                                          (in  8)
"""---^.Fiscal
• ~- Year
"*;•*».
For reclamation
[lor crushing of
residual
1972
3,600
(13,000)
1973
4,260
(21,300)
1974
5,500
(27,500)
1975
6,000
(30,000)
1976
6,670
(33,350)
900
(4,500)
       The amount should be calculated, in principle,  on the
basis of sales revenue from reclaimed material  and  costs for
reclamation, talcing into account proper profit  margins.   Dumping
fees in 1975 were 6,000,000 yen (S30,000)f so that  it  covered
the deficit of the company.

(c)    Comparison between dumping fee and dumping cost in
       ITeda city(1).

       Although the city paid 6,000,000 yen  (§30,000)  to the
company in 1975, it also resulted in the recovery of 2,366 tons
of waste.  By using the cost estimate of waste  treatment,  we
could estimate the saving of municipal expenses for waste dis-
posal under this scheme.

       We use the concept of "dumping cost", i.e. the  amount it
would have cost the municipal authorities if they had  carried
out the waste disposal by themselves without the resources
recovery scheme.

       Out of 3,236 tons of non-combustible  waste generated in
1975, 2,356 tons were recovered and 920 tons were landfilled
after being crushed.  V/e would like to estimate the additional
cost which would be incurred by this increased  volume  of waste
to be landfilled, in terms of (1) additional cost in acquiring
landfill sites, (2) additional cost of digging  and  levelling
the site, (3) cost of additional transportation.

       Ueda city authorities estimate that one  ton  of  waste
needs 3.5 m* of landfill space supposing that the volume reduc-
tion by crushing is 2/3, the net increase in the volume  of waste
to be landfilled is

2,366 ton x 3.5 m5/ton + 920 ton x 3.5 m5/ton x 2/3 =  10,428 m5.
(1) The following calculation is based  on  The_Rcj)_or_t_ _tq ;the
    Japan ^Industrial. Technique Promotion. C'o'*"'
    b"y Su]-:~eTfi'rb""G'o'to and' 3?i";fi "TaVialcaT ""

-------
                                                         4O9
       The depth of a landfill site varies 3^6 m depending on
the conditions of the site.  Therefore, the landfill area needed
for the increased volume of waste to be landfilled is between
1,740 m2 (= 10,488 m? v 6 m) to 3,480 m? (10,428 m  f 3 m).

       Concerning the cost of acquiring a landfill site, Ueda
city paid 1,620 yen/cz2 for the acquisition of the present land-
fill site in 1971.  However, in 1975, the cost would have been
at least 9,260 yen/m2.
caaes:
       Using the above data, talre the following two extreme
r~~~^~~—
'Depth of
{Landfill
r
f
t
-_____^ Cost
site
6 m
3 m
of landfill
jsite (/m2)


1 , 620 yen/in2
(1971 base)
Case I

9,260 yen/m2
(1975 base)

Case II !
i
(1) Sits acquisition cost for Case I 1,740 m2 x 1,620 yen =
    2,618,800 (A)...Yen

    Site acquisition cost for Case II 3,480 m2 x 9,260 yen =
    32,224,800 (A')...Yen

(2) Additional cost of digging and levelling the site is esti-
    mated to be 2,000,000 yen/year...(B)

(3) Cost for additional transportation is estimated to be
    4,565,000 yen...(C)

Therefore, dumping cost would be:

Case I = (A -t- B + C) = 2,818,800 -4 2,000,000 + 4,565,000
                     = 9,383,800 yen ($46,919)

Case II = (A« + B + C) = 32,224,800 + 2,000,000 + 4,565,000
                       = 38,789,800 yen ($193,949)

       On the basis of the above calculation, we could compare
dumping cost, dumping fee (what the city authorities actually
paid for the recycling dealer) and the net cost of the recycling
dealer, we get the following inequalities:
        !Tet cost of the
        recycling dealer
                      Lumping fee
In thousand yen
      (0)

       Dumping co^t
Case- I


Case II
   3,033
(019,165)
   3,333
6,000
(C;30,ooo)
6,000
(G 30, 000)
c
9,33s-
(846,900)
58,790
(0194,000)

-------
                                                          410


ENV/WMP/78.5                 -  14 -
       These inequalities show that the cost  saving  of  the
recycling scheme to Ueda city is larger than  the dumping fee
they paid.  For the private recycling dealer,  the dumping fee
they received covered the net cost so that they were  at least
given positive incentives.  However, further  consideration  is
necessary in order to utilise the capabilities of the private
sector concerning whether the profit to the private  recycling"
dealers  (= dumping fee - net cost) would be enough for  them to
assure their future development.

       (v) Evaluation of the scheme

       A few points can be put forward:

       (a) ITote should be taken of the big effort exerted by
           the company.

       (b) Subsidy by the city authorities to  the firm  worked
           well and helped the viability of the scheme.

       (c) The scheme succeeded in reducing the amount  of waste,
           and contributed to the saving of municipal expendi-
           ture for waste disposal.
       C^pjrtrac t Jbetwe en_ jtjij e^ mun icrga.l, .a u t h o r ity_ jand_ ^a jsrijrate
                 "*  "    "*      ~"    ~~~    "*"
       The next scheme we are going to discuss is a unique con-
trc-.ct made between the municipal authority and a private recycl-
ing dealer.  This is,iin a broader sense, a variation of the
first scheme, i.e. a subsidy to recycling dealers.  The unique-
ness of this scheme is in its bonus payment.  The city pays
the recycling dealer some fixed amount for the operation and
maintenance of the non-combustible v/aste facility.  All the
sales revenue from the reclaimed material becomes the revenue  of
the city.  However, if the sales revenue exceeds the fixed pay-
rjent of the city authorities to the company for the operation
and maintenance of the facility, then the city pays 20 per cent  (
of the difference (excess revenue) as bonus payments.

       The merits of this scheme to the recycling dealer are:

       (a) The recycling dealer has no investment to make for
           the waste management facilities.  As these waste
           management facilities, especially resource recovery
           units are capital intensive, continuously involving
           new technologies, technological and economic risks
           involved make it particularly difficult for a private
           coEroany to build resource recovery facilities.  Thus
           by using the city facilities they can avoid the risk
           of investing in big facilities;

       (b) Since the company receives a fixed payment from the
           city authorities, a minimum profit is ensured so long
           as they keep the cost down;

-------
                                                                  411
                              - 15 -                EHV/UMP/78.5
         (c) If the company is sxiccessful in recovering waste,
            they can get additional payments as bonuses.

         The merits of this scheme to the city are:

         (a) The city authorities can utilise the technical
            expertise of the company in resource recovery.

         (b) Under the bonus payment scheme there is an incentive
            for further resource recovery for the company.

         (c) By contracting out the operation and maintenance of
            the waste management facility,  the city authorities
            are relieved of the administrative burden.

        Let us see Fuchu city as an example of this scheme.

 FUCHtT CJTY (Tokyo Metropolitan Area)  Population 187,000 - 1978

        (i) Background

        Fuchu city used to dispose its final wastes to the land-
 fill sites in the nearby village.   However,  a strong anti-
 landfill movement occurred from residents  living near the land-
 fill sites.

        With this  background,  Fuchu city began construction  of
 "bulky and non-combustible waste treatment facilities"  in
 September 1975 in  order to reduce  waste and  promote resource
 recovery.  The construction was  completed  in March 1975.

        Starting fiscal  year  1976 (April 1976),  Fuchu city made
 a  contract with a  private  company  for the  operation of  this non-
 combustible waste  treatment facility.

        (ii) Municipal waste treatment  in Fuchu  city

        V/aste  collection in Fuchu city is conducted by using so-
 called  "dust-boxes".  There are  two kinds  of dust  boxes,  i.e.
 one  for combustible, the  other for non-combustible  wastes.  The
 frequency of  collection is three times  a week for  combustible
 waste and once a week for non-combustible  waste.

        Collection  of waste is directly  operated by  the munici-
 pality.   Collection of  non-conbustible  waste  is carried out by
 a private  company which has a contract  with  the city  authorities.
 Bulky waste is collected by the municipality  on request.

       All the non-combustible and bulky wastes are  transported
 to the  "bulky and non-combustible waste  treatment facilities"
where recoverable wastes are recovered.  Residuals  are landfilled.

       Combustible wastes are incinerated  and the residual is
landfilled.

-------
                                                                 412
ENV/WMP/78.5
- 16 -
             Th6 following tables (Table VI,  Fig.  IV, Table "VII) show
        the amount of waste collected and the flow of waste disposal.
                                   TABL2 VI

                      The Amount of Waste Collected
                                                                (ton)
" 	 -—. -^.^^^ Year
Type of Waste ~- 	
Collection
by the
Municipality
Combustible
Non-combustible
Combustible waste which is
transported directly to the
incinerator by residents
Total
1972
33,840
7,556
7,833
49,229
1973
33,146
9,144
7,521
49,811
1974
34,307
11,566
6,409
52,282
1975
38,212
11,553
7,074
56,839
1976
40,32?.
6,939
6,987
54,2^8
                               FIGURE IV
    (10,000  tons)
5-
4_
3-
2-
1-

1%
J*s
^
d
,
K
3-
P
r
*
H«
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                          1972   1975 1974 1975  1576"
 ffote; ©  Combustible waste  transported directly by consumer
       Q  Non-conibustible v/aste
       Q  Combustible waste

-------
                                  -  17 -
          413




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                                                        414
 ENV/WMP/73.5                -  18  -
       (iii)  Contract  between  city "authority and  the  private
             recycling company with  respect to  resource  recovery

       The  "bulky and  non-combustible waste treatment facilities"
 are  operated by a firm under  contract with Puchu city (after
 bidding).  This contract  characterises  the scheme.   The
 essence  of the  contract is:

       (a)  The city pays the conroany for the operation and main-
           tenance of  the  facility /Tn PI 1977, 1,660,000 yen
           (&8,300)/month  or about 20",000,000 yen ($100,000)/year/.

       (b)  The company makes every effort to recover  material
           from  the  waste  transported to this facility (there is
           no specification of the amount to be recovered).

       (c)  The cost  for electricity, water supply and maintenance
           of the  facility is  borne  by the municipality.

       (d)  All sales revenue from the recovered material goes
           to the  city authorities.

       (e)  If the  sales  revenue exceeds  the fixed payment by
           the city  to the firm for  the  operation and maintenance
           then  the  city will  pay 20 per cent of  the  difference
           to the  company  as bonus payments.

       (f)  Recovered material  should be  sold to dealers  other
           than  the  one  which  operates the facility.

       (iv) Costs  and  effects  of resource  recovery

       (a)  The amount  of material recovered.

       It can be seen  in Table VIII  that  in 1976  30 per cent  of
the waste  brought to  this facility  is recovered  and  in  1977
(11 months)  37.8 per  cent is  recovered.   In monetary terms,  in
1976 they  sold  14,738,000 yen (373,690) /about 1,230,000 yen
(06,150) per month?.   In  1977 (11 months; they sold
25,334,000 yen  (#T26,670) /about 2,300,000 yen ($11,500) per
month/.  In  1976, monthly payments  from  the city to  the fim
were~1,490,000 yen  (87,4-50; and in  1977  1,660,000 yen (£8,300).
Therefore, in 1977 monthly sales revenue  exceeds monthly payment
from the city to  the  firm for about 640,000 yen  ($53,200;.

       (b)  The costs for treatment of non-combustible  v/aste.

      Based  on  the fiscal 1977 budget and results of  the amount
of non-combustible v/aste collected and  the amount recovered,  we
could estimate the costs for  collecting non-combustible waste
and treatment (see Table IX).

      According to the  FY 1977 budget,  the cost  for  collecting
non-combustible waste  is 49,700,000 yen  ($24,850) and operating
and maintenance cost  for the  "non-combustible and bulky v/aste

-------
                                   415
- 19  -
EIIV/V.:-IP/73.5
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                                                      416
EKV/VMP/78.5
- 20 -
•ireavment facility" is 30,360.000 yen (5151,000).   (This  excludes
depreciation of the facility.)  Assuming that the salary  of  one
municipal employee (who supervises the disposal facility) is
4,500,000 yen (&22,500)/year, then operating and maintenance  cost
for the treatment facility amounts to 34,860,000 yen  ($174,300).


                           Table, IX

        COSTS FOR ITON-COMBUSTIBLE WASTE COLLECTI01I  A1TD
                          TREATMENT
                                             (Direct costs  only)
                                                  FY 1977
i | Cost (1,000
• f yen )
; (dollars)
; 1. Collection(4)
!
49,700
( §24, 850)
J t
X _____ _ 	 ^ 	 	 _ 	 	 . J _
Amount (ton)
•
•7,547t(D


: 2. I;o:.- -combustible '
! Waste Treatment
j Facility
! (a) Operation &


30, .-360
\ maintenance \ ($151,800)
I cost f
r k
' (b) labour f 4,500
| [ (§22,500)
| (c) Bonus | 1,520(3
| payment ( ($7,600)
i Sub-total I 36,330
[ (5181,900)
(d) Sales
; revenue
3. Net Cost
-27,600
($-138,000


I ,

4
• <

F
I
| 8,062t(2)






8,780
(043; 900)



I Per ton •
(yen) j
(dollars) [
• 6,585
i (§32.9
•f
C n 	
f j
it *
f

)

) t
k
> i
i
4,512
f (C22.6) j
> ' *
{ I
j



i
r
-3,423 I
($-17.1)

1,089 j
(55.45) j
1-Iote:  Figures in April 1977 to February 1978 are actual "results,
       For 1978,  same figures as for 1977 used.

(1) Only non-combustible waste.

(2) Inclusive of non-combustible and bullry waste.

(3) (27,600,000 - 20,000,000) x 0.2.

(4) Exclusive of depreciation of dust boxes.

-------
                                                          417
                             -  21  -
          ENV/WMP/78.5
        The  amount of non-combustible waste  collected  and  treated
 In the  disposal  facility is  7,547  tons.   (If  we  include "bulky
 waste treated at the facility,  then it  is 8,062  tons.)  There-
 fore, unit  cost  for collecting  non-combustible waste  is
 6,585 yen/ton (S32.9) (= 49,700,000 yen T 7.547  ton).

        The  sales revenue is  about  2,300,000 yen  ($11,500)  per
 month,  i.e.  27,600,000 yen (:.;i38,000)/year.   Sales .per unit  ton
 is 3,423 yen (S17.1) (=  27,600,000 * 8.062  ton).  Bonus payment
 is 1,520,000 yen (?.7,600) (= 27,600,000 - 20,000,000  x 0.2).
 Therefore,  net expenditure by the  city  is 8,730,000 yen
 (043,900) and 1,089 yen  (05.45)/ton.

        (c)  Other costs for waste treatment.

        Estimation of other costs for waste  treatment  on the
 basis of IT 1977 budget  and  the result  of the amount  disposed.
 of is given in Table X,  which is in terns of  yen  (

                           Table X
! Collection of Collection of
Combustible \ llon-comtus-
Waste | tible waste
Incineration
landfill
10,255 yen/ton! 7, 290 yen/ton j 5,537 yen/ton ; 3,470 yen/ton
(£51.3) I ($36.5) ! ($27.7) j ($17.4)
                                                             ^-4-

                                                               k
                                                               k


llote:   (1) Collection cost = budget appropriation  for  collection
           + depreciation cost  of collection vehicles.

        (2) Collection cost of non-combustible waste includes
           depreciation cost of dust boxes.

        (3) Landfill cost = labour cost  (two employees) + depre-
           ciation cost of vehicles (container, bulldozer,  etc.)
           + site development.  (Site development  here means
           only actual construction or  digging etc. and does
           not include the cost for purchasing the site or
           compensation).

        (v) An evaluation of the system
       Table VIII shows that 2,801 tons
claimed in FY 1977 (11 months) which is
for landfill.  Prom Table X can be seen
landfill is estimated to be 3,470 yen  ((;;
figures we can presumably calculate the
by waste reduction, i.e. 9,740,290 yen (
= 9,740,290).  It can be seen that this
the net expenditure by the city for non-
ment 2^,780,000 yen (043,900J7.  (See T
of waste has been re-
the reduction of waste
that the unit cost of
17.4)/ton.  From these
saving of landfill cost
•(,;;43,701) (3,470 x 2,807
figure is greater than
combustible waste treat-
.tie IV.)

-------
                                                         413


 E1TV/1MP/78.5                 - 22 -
        Although this cost saving is quite modest and may be
 arguable, we could at least say that this scheme is economically
 viable.  Moreover, by introducing this scheme, the city has
 attained substantial reduction of waste material and reclamation
 of used material which is of course environmentally desirable.
             JrLs.JL-Q.:L.a. JfcUAic ABal.lj. owned. . Jlr-OAeAsinjL. Jfec.^Aty.. bv.
        This section also deals with another variation of subsidy
 to recycling dealers.

        A commercial recycling dealer is allowed to use a munici-
 pally owned waste processing facility but he does not pay any
 fee to the municipality and the municipality pays no charge for
 the processing service.   The dealer just makes a profit by selling
 recovered material.

        As we have discussed in the  previous section,  investment
 in waste processing facility involves technical and economic
 risks.   By using the facility of the municipality free of charge,
 the private company can  avoid such  risks.   Therefore,  this scheme
 can essentially be thought  of as a  variation of a subsidy
 scheme.

        We will explain briefly the  example  of Shiki District
 Hygiene  Association.

        Shiki District Hygiene Association:   Population about
 250,000" -~ ^^TfT^^^Asso'(^^^''i^^e"^ier-immicipal agency
 formed  by three  cities - Shiki,  JTiiza'and Fujimi.)

        In order  topprotect  waste incineration furnaces,  separate
 collection of combustible and non-combustible wastes  started
 in  1969.   At this  tine the  system was  designed so that combustible
 wastes  collected  by each city were  incinerated by the  Association
 and non-combustible wastes  were  used as  landfill  by each city.
 However,  shortage  of landfill sites  made this plan  difficult.
 Consequently,  the  Association started  recovering  material from
 non-combustible waste in 1970 in order to reduce  the amount of
 waste to  be  landfilled.

       Bottles, glass and metals  are recycled.  Such items  are
 separated  at  source and  collected by exclusive  trucks  and trans-
 ported to  the  sorting lot.  Collection  is directly  operated by
 each city.   Processing and  disposal  are  operated  by the
Association.  A commercial  salvage dealer extracts, crushes and/
 or presses bottles, glass and metals at  the  facility of  the
Association.  The  dealer does not pay  a  fee  to  the  Association,
and the Association pays no fee  for  the processing  service.
The dealer has to manage by himself  from the  profit he makes in
 selling recovered material.

-------
                              419
- 23 -
EITVAMP/78.5



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/ :
/ g ]
~
CO
to
to
I-
:?
to
^"
§i
«i:
T—
c- ;
o
T—
VO
CM
^ 	
gi
-i
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1
I
Metalsd)
CM
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0
CM
^
in
o
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*•
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to
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vo
*•
o
^J-
co
in
_r ;
«
CM
c-
j
0 {
^
]
•
T.^*4.-«J Recovered
BottxeslAmount

in
to
CM"
CM
£
»*
CM
O
CJ
^
c7
L j
vo
in
"i
CM
1
CM
VO
co ;
- ;
«
CM
?-
T—
O
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biass j collected
j Amount
to
to
cn
i °
in
to
~
oT
CM
cn
CO
in
cn
to
CM
CM
0
o-
to
CO
cn
^
$ i
&
t^>
to^
to
t<^
J i
~ !
Total amount of
v/aste collected

in
vo
S
1
s
*
I
s
I>
in
•5
c-
• 1
f-
'
4
cn ;
to
in
i
00
to
o
9:
V— f
S]
+ |^ ;
• ^
cr i i
~! 1
4
J
O
H
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4 _,
1
CO
!frt
c
0)
CO
H >>
CO
•P H
CD C3
S o
03
0 
-------
ENV/WMP/78.5
                             - 24 -
        The amount recovered since 1970 is shown in Table XI.
 As for metals, the amount collected separately almost equals
 the amount recovered.  Regarding bottles and glass, the ratio of
recovery
                             ls 50 per oeat ^ao per oent.  tte
 ratio of the amount of recovered material to the total amount
 of waste collected is 7.3 per cent in 1975 and 5.6 per cent in
 1976.  The decline in 1976 is due to the fact that in 1976
 Shilci city contracted out the collection of non-combustible
 waste so that less recoverable waste was transported to the
 Association.

        Sales revenue from recovered material becomes that of
 the dealer.   The dealer finances with this revenue the costs
 for processing and recovering.  He receives no financial help
 from the municipality.   Table XII shows the sales revenue.
              R.ev_enue_, jfjcojnj5al.es, jxC, .Rejc^ove^A frfest-6-
                                                  In thousand yen
                                                   (in dollars)
IX
!  \
jltem\

iMetal
1970
                    1971
          1,050 ,   1,410
 1972

— - — -iT -fc r-

4,600
1973
                                                1974
                                                            1975
                                       5,590     12,360 |    7,940
                                     ($27,950)(61,800) (©39,700)
Bottles
              0    2,030 (   6,370
                !*,*<. A * . _—...*,.  '
                                       6,990
                                      ..  *  _ _
                                       9,150
                                                            8,070
                   C.% \JJ\J    V } 3 I U   '  U,^^W      ^, I jv     V, v I v  '
                (e-10,150) j (031,850)'(034,950)! (045,750)  (540,350)

Total   i  1,050 .   3,440 I  10,970   i 12,580  '< •      :      16,010
        KG5,250X017,200)| ($54,850) ;(f,62,900)^107,55- ;| (080,050)
       In  order.to promote recycling and  resource  recovery,
Hiratsuka  city purchases recoverable wastes  from voluntary
citizen groups at a price somewhat higher than  the market price.
The city then sells it  to secondary  material dea.l^v  :t the
current market price.   Thus the city authority  g.i,    m economic
incentive  for group collection of recoverable waste.   This
scheme can be thought of as subsidies  to  voluntary citizen
groups for their recycling activities.

SIM^IUiL^JL^1  Copulation about 200,000

       (i) Background

       As urbanisation  proceeded, it became  increasingly diffi-
cult to secure landfill sites in Hiratsuka city.   Beginning
Hay .974, city authorities started reducing  waste  by  using
crushers, recovering ferrous metal from non-combustible and
bulky waste, and incineration of combustible waste.

-------
                                                         421

                             - 25 -                 EFV/Y/MP/78.5
        In order to further reduce waste and encourage reclamation,
 Hiratsulca city started a new scheme in April 1975.   The new
 scheme which Hiratsuka city introduced is as follows:  the city
 buys recoverable waste from citizen groups at a price somewhat
 higher than the market price.   The city then sells  it to secon-
 dary material dealers at the existing market price.  Secondary
 material dealers collect recoverable waste at the time and place
 agreed upon in consultation with the city authorities, local
 community groups and the dealers.

        This scheme was originally proposed by a municipal per-
 sonnel engaged in waste management.  The mayor was  interested
 in the idea and consequently it was implemented.

        (ii) Municipal waste treatment in Hiratsuka  city

        In Hiratsulca city,  municipal waste is segregated at
 source into two types,  namely  "combustible"  and "non-combustible
 or bulky" waste.   The collection and transportation of waste is
 directly operated by the city  authority.   Combustible waste is
 incinerated,  the  residual  of which is landfilled.   Hon-combustible
 waste  is first crushed,  then ferrous metal is magnetically
 extracted and recovered,  the remainder of which is  separated in-
 to combustible and non-combustible waste.  Combustible waste
 is then incinerated,  and non-combustible  waste is landfilled.

        Besides the routine  collection and disposal  of municipal
 waste  by city authorities,  which we have  just described above,
 there  is s  scheme  for group collection of recoverable waste and
 which  is discussed in detail in the next  section.

        The  flow-chart on v/aste  management in Hiratsulca city is
 given  in Table XIII.

        (iii)  Detailed description of the  scheme  - group collection
              of recoverable  waste.

        In Hiratsulca  city, any local group (such  as  municipal
 groups,  parents' and  teachers'  Associations,  children's groups,
 senior  citizens' groups, housewives'  groups  etc.) can register
 as an agent for group collection  of recoverable  waste.   There
 are  139  such  citizen  groups  registered  (lloveinber 1976).

        The  time and place of collection of recoverable v/aste
 is decided upon at a  consultation  meeting  between the  city  autho-
 rities,  local  citizens' groups  and the dealers.

       For  residents  of Hiratsuka  city, this  scheme  (purchase  of
 recoverable waste by  city authorities) is  basically  the  same
as ordinary group collection.  However, the  city authority  is
involved in the group collection  in  the following fashion.

       First,  the city authority helps citizens' groups  to  co-
ordinate with dealers.  As well city personnel go to  the  spot
of measuring waste.

-------
                                                                                    422
  ENY/WMP/78.5
-  26 -
Resource Final
Hecoverv Disposal!
eatment
Intermediate Tr
Landfill
Resource
Recovery
Incineration'
ortine; .
Mechanical
c
Manual
Collection
Transportation
Discharge
Segregation
\ to
o \
1—1 \











, cO -P
W 3 X I* 0
!3 & i — 1  4) 3 rH
E 0 P2 0 -P 0 H
O O O W ft O
U 1 0) jO U U
_o



to
-p
c
cO
-p
•H
,£>
ca
c
>-i
c

c




1 	 w !
Crushing
n

—
03
^3
•P
Combu

u.
r~
^
^j
bar
•r-jC
•PS
tK3
CC
0£
^Magnet


'
H
H
•H
VI
«
C
.3





s



Municipal
Authority



to
H
as
53
to
3
CD
fc


C





5

Private Firms
(Collection
Transportation
licclama tion)








Recovered
Mn terial
User
 -p
 •H
 O

 03

 3
 to
 -p
 tO
 •P
 C
 0)
 £
 (D
 bO
 cu
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 O

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 k
 CO
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 o
 s
 o
rH

-------
                             - 27 -
                                                      423


                                               EirV/VMP/78.5
        Second, the city authorities buy recoverable waste from
 citizen groups at a higher price than the market price, which
 means that the citizen groups are able to make better deals.

        The categories of waste purchased by the city authorities
 are:  waste paper (newspapers, magazines, cardboard;, reusable
 bottles, cans, ferrous metals and clothes.

        Frequencies of collection depend on the situation of each
 group - 4/'x-'5 times a year in the active groups.

        The collection and transportation of recoverable wastes
 are conducted by commercial recycling dealers.

        The flow chart of the procedure of this scheme is given
 in Figure V.
 1.
     (iv)  Costs  and effects of group collection of recoverable
          waste

     Effects
        The amount recovered between April 1977 to 1-Tovember 1977
 (nine months)  was 770 tons.
I • • •' *
i
I Paper
Magazines
j Bottles
j Ferrous
| metal
Clothes
Total
Amount Purchased
(kg)
402,323
107,699
94,012
123,395
42,794
770,228
Percentage
I
!
52#
14^
12^
I6?o
6$
100# \
          139  groups  participated
          2§0  collections made
2.
    .Costs for resource, recovery
       (a) Cost  of purchasing  recoverable  waste
       The city paid 8 yen/leg  (£.40/ton)  for the  purchase of
recove'rable waste from citizen  groups  irrespective  of the con-
tents.  The city then sold  the  recoverable  waste to the  dealers
the current market pric
betv:ee:: July and September 1977 was:
                              The current  ui~.it  market  price

-------
                                                                 424
ENY/WMP/78.5
                         -  28 -
  FIGURE V  : -FLOW CHART OF GROUP COLLECTION OF R5COV5RABL3 WASTES
Local
Citizens'
GrouD
                  Public
                  Relations
                Decide the place

                for collection
e.g.
Municipal Group
P.T.A.
Senior Citizens'
Grout)
In order to get
better understanding
and cooperation of
as many people as
possible, they ask
for the cooperation
of such organisations
as local community
groups
          City Authority
Pay on the y&asis
of estimated price
or standarA price
(which ev/r is
 higher)
   Local
   Citizens'
   Groups
                Pay on the
                basis of
                estimated
                price
              Dealers
                  The group ir.fonns
                  city authority of
                  the date and place
                  of collection
           'City,  dealers
           local  groups {
                         Measurement
                         of Waste
                                       City authority informs
                                       dealers'  association
                                       of the time and Dlace

-------
                               - 29 -
                                                      425


                                             EiTV/l/MP/78.5
        Cardboard,  newspapers
        Magazines
        Reusable bottles
        Ferrous metals
        Clothes
                              8 yen/kg
                              4
                              3
                              3
                             15
        The flow of money for purchasing recoverable waste between
 April  1977 to November 1977 is shown below:
 Local  citizen
 Groups
Recoverable waste 770 tons

           ' —--—""Y476"35","2
                  (523,176)
-j i x >jt—M.--*»ym, • i .» i •—*_u
 ¥^,16TTS24
 (§•30,809)
           (¥8,000/ton)r«-
           (320/ton)
                                      (¥6,018/ton)
                                      (830/ton)
                                               Secondary
                                               Material
                                               Dealers
        City  authorities  paid  the  difference of ¥1,526,593 (^7,633)
 or ¥1,982/ton  (.^9.9/ton).
        (b) Costs  for  disposing  of waste
                                                        1976

Collection and
Transportation
Incineration
Crushing
; landfill
,
(ton)
Amount Treated
54,980
54,668
9,031
17,464
(thousand yen)
Costs for
Treatment
1
538,079
(32,690)
146,266
(0731)
65,060
($325)
22,590
(;,113)
Costs for I
Treatment/ton
Yen U)
9,787
($48.9)
2,^676
7,163
(i35.8)
J''233)
V. it1 « -? /
3.
Evaluation of costs and effects
       (a) The city authorities paid  1,932 yen  (09.9)/ton  for
purchasing recoverable wcste.  However, at the  same  tine,  they
saved the costs of collection, transportation,  incineration  and
landfill for combustible waste, i.e.  13,756 yen (C.68.8)/tor
(= 9,737 yen + 2,676 yen + 1,293 yen).  For non-combustible
waste they saved the costs of collection  transportation, crushing
and landfill, i.e. 10,244 (091)/ton (= 9,737  +  7,163 +  1,295).
              The weight reduction of waste  in  the  incineration
process has not been taken, into account.  Cost  savings have  been
calculated as if all the ucste collected had gor.e directly for
landfill.  Although this is conewhct overestimated ,  the  over-
estimation does not affect the overall evaluation very Liueh.

-------
                                                     426
 ENV/UMP/78.5                - .30  -
        The  actual  amount  of  recoverable waste purchased  in
 FY 1977 was 1,204  ton and of that 70 per cent was combustible,
 the  rest was non-combustible, thus the total saving would amount
 to 18,183,283 yen  ($90,916).

 Note;   1,204 tona  x 0.7 x ¥13,756 = ¥11,593,556
        1,204 tons  x 0.3 x ¥18,244 = ¥^£
                                    ¥18,183,288

 The net  saving would be ¥15,796,960 (£78,953).

 .Note:  18,183,288 - 1,982 x 1,204 = 15,796,960
                       (78,935)

       (b) Effects on waste 'reduction

       Since the total weight of waste collected in FY 1977 is
 56,167 tons, the ratio of waste recovered by this group collec- •
 tion scheme is 2.1 per cent.  This does not seem very much.
 However, we have to note that this has been conducted by the
 activity of voluntary groups.  (Other than this group collection
 scheme,  1',016 tons of ferrous metal is recovered at the muni-
 cipally  owned crushing facility.)

       (c) The city authorities give an economic incentive
           for group collection of recoverable waste by purchas-
           ing it at a price somewhat higher than the market price,
           The local citizen groups benefit by this scheme
           as they can get the difference between the price
           offered by the city and the existing market price.
           Between April to ITovember 1977, about 1,500,000 yen
           (07,500) was redistributed to the local citizen-
           groups , the resource for which is of course tax
           collected from residents.

       How to evaruate this income redistribution effect?  If
we consider the activities carried out by the local citizen
 groups simply as discharge of waste, then it would not be
acceptable to give economic incentives.  However, since their
activities contribute to the reduction of waste and consequently
 saving of municipal expenditure for waste disposal, it would be
Appropriate to regard their activitias as pollution abatement
activities, so that subsidies to these local citizen groups
would be justifiable.

       (v) Evaluation of the scheme

       In this scheme, the role played by voluntary groups should
be highly evaluated.

       Secondly, by the co-operation of voluntary citizen groups
and the association of recycling dealers, this scheme, to date
succeeded in saving municipal expenditure for waste management.

-------
                                                           427


                                                  EI7V/WMP/78.5
III.   COITCLUSIOTTR

       In principle, recycling should be promoted.  In practice,
however, there are differences in its logic for residents, pri-
vate firms, municipalities and the national government.  What
role should each participant play and what kind of economic
system should "be sought?  Japanese municipal experiences,
although recent phenomena, give some -insight to these questions.

       (i) Introduction of various resource recovery schemes
           started in response to crisis situations rather than
           as a considered response to cost reduction possi-
           bilities.  However, some cities achieved modest, if
           not dramatic, cost savings as a result of the schemes.
           (llote here that there are difficulties in cost com-
           parisons as municipal budget and expenditure data
           do not represent,the full economic cost of resources
           devoted to waste management due to the accounting
           practices).

           Introduction of various schemes stimulated overall
           reassessment of waste management administration as
           well as reorientation of environmental administration
           as a whole.  It is also reported that the conscious-
           ness of civil servants engaged in waste collection
           and management is seen as well as the increased
           awareness of citizens concerning resource reoovery.

      (ii) The schemes employed, vary from one city to another
           depending on local circui-istances.  Factors which
           might affect the schemes and the choice of organi-
           sation as well as economic viability of these schemes
           are:

           (a) the availability and competence of recycling
               dealers;

           (b) the level of public participation,  especially
               voluntary activities from citisen groups;

           (c) the level of source segregation;

           (d) the availability of landfill sites;

           (e) secondary material marlcet situation.

     (iii) The utilisation of expertise of private recycling
           firms should be er.couraged.   The choice of the scheme
           or the choice of the organisation depends on local
           circumstances.   It is reported that in Ilatano city
           an innovative recycling dealer,  without any help
           from city authorities v/as very successful in collect-
           ing and recycling recoverable waste.  They have
           collected and recovered about 10 per cent of
           the total amount of waste collected in the city.
           Therefore,  whether subsidy of any form is necessary or
           not depends on  the local situation.

-------
                                                           428

EH7/WMP/78.5                - 32 -
      (iv) All the successful experiences found v/ere in the
           medium or small sized cities.  The applicability
           of the experiences into big cities should be con-
           sidered, together with its possible impact on secon-
           dary material markets.

       (v) The role of central government in encouraging these
           schemes should be sought.  Information and experience
           could be collected and disseminated by setting up a
           model city and undertaking a pilot project.

      (vi) Japanese experiences heavily depend on unique
           Japanese circumstances such as shortage of landfill
           sites and severe pollution regulations.  However,
           other Member countries may face similar situations
           in the near future as we have seen in California,
           In that sense there are lessons to be learnt from
           Japanese experiences.

-------
                                                 429


                            - 33 -                ENV/WIP/7S.5
1.   .  Brief Report of Source Separation in Japan, Eiji Tanaka.
     •  Do Tank Dynacs Co. Ltd., Tokyo.  June 1973.

2.     Shigenlca Handbook (Handbook for Resource Recovery).
       Haikibutsu Shigenka Kenkyukai  (Stud3>- Group for the
       Resource Recovery from Waste).  Tokyo.  March 1978.

3.     The Privatisation of Public Services:  Solid Waste and
       Waste Water Disposal, Suraner Myers et al.,
       El-nr/URB-US/78.104.

4.     Financing of Municipal Services Collecting Household and
       Allied Types of Waste, Alain Chambournier,
       E1TV/ZJRB-US/107.

5.     Municipal Waste:  Economic Aspects of Technological
       Alternatives, Joan Wilcox in Resource Convervation,
       Social and Economic Dimensions of Recycling, edited by
       David W. Pearce and Ingo Walter, Hev.r York,  1977.

6.     The Economics of Refuse Collection, P. Semper and
       J.M. Quigley, Cambridge, Mass. 1976.

7.     Resource Recovery from Post-consumer Waste in Japan,
       Kunitoshi Sakurai.  Paper presented to the third
       Ja nan -U.S. Conference on Solid Waste Management, May
       1976, Tokyo.

8.     The Report to the Japan Industrial Technique Promotion
       Co-operation, S. Goto and E. Tanaka, 1976.*

-------
                                                     430





            STATE SOLID WASTE MANAGEMENT 'PLANS




                    Georcje A. Garland



               Office of Solid Waste, EPA








     The following paper is excerpted from the U.S.-EPA



Guidelines for Development and Implementation of State Solid



Waste Management Plans proposed in the Federal Register




August 28, 1978 (copy enclosed).   Public comments were



solicitated throughout the nation and the final guidelines will



be published in June 1979   We welcome any comments and



discussion by the Japanese government on the scope, definitions



and management aspects of the proposed rules.  There are» a number



of important issues raised by these proposed guidelines.   Three



of these issues, discussed below, are abandoned sites, State



and substate agency roles in facility planning and implementation,



and resource conservation and recovery.








     Abandoned facilities.  Abandoned, inactive disposal



facilities have caused significant adverse health and



environmental effects.  Therefore, these guidelines state



that abandoned facilities that continue  to produce such effects



are subject to State regulation and corrective action.  The



State plan need not provide for Statewide surveillance and



monitoring to determine locations of all abandoned facilities;



rather, the investifation of abandoned facilities should be



directed at those sites with a high potential for causing severe




health or environmental problems, such as leachate contamination

-------
                                                       431




of drinking water supplies and explosions from accumlated



gases.








     It is recognized that it may be very difficult to take




enforcement action with respect to abandoned facilities



because ownership may have been transferred or relinquished,



and legal liability and financial responsibility may be




difficult to establish.  Therefore, if corrective actions by



facility owners or operators cannot be brought about, public



agencies should take necessary measures to protect public



health and safety.  This should include, as a minimum,




notification* of adjacent residents and other affected parties



of the potential health or environmental hazards.








     Recognizing the difficulties of correcting or upgrading



abandoned facilities, preventive measures should be taken



before facilities become inactive.  The guidelines require



the State plan to provide* for facility closure procedures to



eliminate or minimize adverse health or environmental effects.



Facility owners or operators should be required to comply



with such procedures through the facility permit or registration.








     State and substate agency responsibilities for facility



planning and implementation.   These guidelines require that




the State plan provide for adequate resource recovery and




disposal facilities and practices necessary to use or dispose




of solid waste in an environmentally sound manner.  These

-------
                                                     432




guidelines also recommend a number of actions that could be




undertaken to help assure that the necessary facilities and



services are in fact provided for.








     In complying with this requirement,  it is important to



strike an appropriate balence between public and private



sector activities.  These guidelines do not favor one over




the other.  In some parts of the country,  private sector



initiatives may be sufficient to insure that the needed



facilities are available.  However, in other instances,




there may be a need for greater involvement should include




an awareness of private sector activities  in order to determine



whether public sector involvement in facility planning and



implementation is necessary.








     EPA 'recognizes that there is an established solid waste




management industry offering a wide range  of services,



including the design, construction, and operation of processing,



treatment, transport, disposal, and recovery facilities.   It



is not the intent of these guidelines that teh public sector



needlessly supplant or duplicate activities of the private



sector.  State and substate agencies are  encouraged to establish



policies for free and unrestricted movement of solid waste across



jurisdictional boundaries and procedures  for sharing information




useful to prospective and established entrepreneurs, as well as




to provide relevant planning information  to industry regarding




population and waste generation trends, environmental conditions

-------
                                                       433
and other topics that would assist in the establishment of
financially and environmentally sound facilities.


     The guidelines recommend a Statewide assessment of the
adequacy of existing facilities and an evaluation  of the need
for new or expanded facilities.  The guidelines purposely leave
it up to State discretion whether this needs assessment is to
be conducted by State or substate agencies or by a combination
of the two.  Where facilities and practices are found to be
inadequate, actions should be taken to help ensure that needed
facilities are developed by State or substate agencies or by
the private sector.  For areas found to have five  or fewer years
of capacity remaining, more detailed  planned should be carried
out, including evaluation of technologies and site locations.
Implementation schedules also should be developed.


     Where there is less than two years' projected capacity,
teh State should have the authority to acquire facilities or
cause facilities to be acquired..  It is recognized that facility
acquisition activities have traditionally been the responsibility
of regional and local governments.  However, recent experience
indicates that it is becoming more and more difficult for
substate governments to obtain sites for solid waste disposal
facilities.  This is especially true for facilities that store,
treat, or dispose of hazardous wastes.  Therefore, it is
important for the State plan to explore options for more direct
State control over siting and facility development if local

-------
                                                     434

government and private sector initiatives fail.   EPA invites

comment on methods .for the State to obtain greater control

over facility acquisition; such methods could include obtaining

the authority to override local zoning law's or to contract

directly for facilities and services,  requiring facility

permits to conform to regional plans developed under the

State plan, or instituting a public utility agency to regulate

the supply of services.



     Resource conservation and recovery.  One of the major

objectives of the guidelines is to encourage resource recovery

and resource conservation.  These terms are defined as

follows:



     Resource recovery:  The recovery of material' and energy
     from solid waste.
     Resource conservation:  The reduction of the amounts of
     solid waste that are generated, the reduction of overall
     resource consumption, and the utilization of recovered
     resources.


These guidelines establish several requirements for State plans

directed toward achieving this objective.



     The guidelines require the State plan to provide for the

development of a policy and strategy to encourage resource

recovery and resource conservation.  This strategy should focus

on removing existing technical, economic, and institutional

constraints that impede increased resource recovery and conservation

State activities in this area could include technical assistance,

training, information development and dissemination, financial

-------
                                                         435





  support programs,  and  programs  to  develop markets  for  recovered



  materials and  energy.








       The Act requires  State  plans  to  ensure  that local



  governments  are  not  prohibited  under  State or  local  law from




  entering into  long-term contracts  for supplying solid  waste



  to resource  recovery facilities.   This section reflects the




  concern that the development of resource recovery  facilities



  has been hindered  by restrictive procurement laws.   The




  guidelines recommend that  the State plan provide for State



  agency review  of pertinent State and  local statutes, and  for



  the development  of a strategy for  eliminating  the  long-term



  contracting  restrictions.  It is recognized that States and



  State agencies may have limited ability to modify  local



  procurement  laws.  Therefore, cooperation of local governments



  and public education and participation are important in



  meeting this requirement.








       The guidelines  require  State  agencies to  purchase items



  composed of  the  highest percentage of  recovered materials



  practicable, whenever  Federal funds are used for such  purchases.



  These guidelines allow States to delay in complying  with



  this requirement until EPA issues  additional guidelines




  which will recommend procedures for purchasing recovered




  materials and  provide  information  on  their availability and




  uses.   These guidelines  also  recommend that the State plan




  provide for  the  development  of  a policy to encourage procurement




.  of  recovered materials and examination of potential uses of

-------
                                                        436





recovered materials by State purchasing agencies.








     It is recognized that State solid waste management




agencies are generally not involved in procurement practices



and policies. Therefore,  the State plan should indentify the



agencies with responsibility in this area and provide for



the necessary actions by such agencies in order to meet this



requirement.








     The guidelines recommend resource recovery and resource




conservation as the preferred methods of solidwaste management



whenever technically and economically feasible. While



resource recovery and conservation may reduce land disposal




needs, however, these methods will not eliminate the need



for land disposal.  It is expected that in the near future,



resource recovery and conservation will have only  a limited



impact on the solid waste generated nationwide. Therefore,



there will continue to be a need for environmentally sound



land disposal facilities in order to meet the objectives of



the Act.

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 MONDAY, AUGUST 28, 1978
       PART IV
ENVIRONMENTAL
   PROTECTION
     AGENCY
STATE SOLID WASTE
MANAGEMENT PLANS

     Guidelines for
    Development and
     Implementation

-------
 38534
          PROPOSED  RULES
 [6560-01J

    ENVIRONMENTAL PROTECTION
               AGENCY

            [40 CFR Part 256]

              [FRL 922-1]

 GUIDELINES FOR DEVELOPMENT AND IMPLE-
  MENTATION OF STATE SOLID WASTE MAN-
  AGEMENT PLANS

 AGENCY:  Environmental Protection
 Agency. (EPA).
 ACTION: Proposed rule.
 SUMMARY: This proposed regulation
 contains  guidelines  for  the develop-
 ment  and  implementation  of  State
 solid waste management plans.  These
 guidelines  are  required  by section
 4002(b) of  the Solid Waste Disposal
 Act, as amended by the Resource Con-
 servation and Recovery Act of 1976
 (the "Act"). States are eligible  to  re-
 ceive financial assistance  under subti-
 tle D of the Act if the State plan has
 been approved by EPA. This proposed
 regulation  establishes  the  require-
 ments  for  State  plans  and recom-
 mends  methods  and  procedures  to
 meet those requirements.  As set forth
 in the Act, the  State plan must pro-
 vide for  the identification   of  State,
 local, and regional responsibilities for
 solid waste management,  the encour-
 agement of resource recovery and con-
 servation and the application and en-
 forcement of  environmentally  sound
 disposal practices.
 DATE: Comments must be received on
 or before November 27,1978.
 ADDRESS: The mailing  address for
 all comments is Office of  Solid Waste
 (WH-564),  Environmental Protection
 Agency,  401 M Street SW.,  Washing-
 ton, D.C.  20460, Attention: Mr. George
 Garland,  docket 4002(b).
  Public  hearing  and  meetings:  A
 public hearing will be held on October
 26,  1978,  at the  Main  Auditorium,
 General   Services   Administration
 Building,  18th and  P  Streets  NW.,
 Washington, D.C., from  9 a.m. to 5
 p.m.; registration at 8:30 a.m.
. Ten public meetings will be held on
 the dates and at the locations shown
 below. The public meetings will consist
 of  a presentation  on  the   proposed
 guidelines,  followed  by  a discussion
 session.

        Date, time, and location
 September 13, 1978, 1 to 5 p.m.  and 7 to 9
  p.m.. Radisson Muehlebach  Hotel, Towers
  Room 22,  12th  and  Baltimore Streets,
  Kansas City, Mo.
 September 18, 1978, 9 a.m. to 3  p.m., EPA
  Regional  Office,  1200  Sixth Avenue,
  Room 12-A, Seattle, Wash.
 September 19. 1978, 1 to 5 p.m.  and 7 to 9
  p.m., EPA Regional Office, 215 Fremont
  Street, Sixth Floor, Nevada  Conference
  Room, San Francisco, Calif.
September 21, 1978. 9 a.m. to 3 p.m., EPA
  Regional Office, 1860 Lincoln Street, Elm
  Room, Ninth Floor. Denver, Colo.
September 26, 1978, 9 a.m. to 3 p.m., Shera-
  ton  Biltmore, 817 West Peachtree Street
  NE., Atlanta, Ga.
October 4, 1978. 10 a.m. to 3:30 p.m., Conti-
  nental Plaza Hotel,  909 North Michigan
  Avenue, Windsor Room, Chicago, 111.
October 5, 1978, 9 a.m.  to 3 p.m.. Ford Foun-
  dation, 320 East 43d Street, New York,
  N.Y.
October 11, 1978, 9 a.m. to 3 p.m., EPA Re-
  gional Office, John  F. Kennedy Federal
  Building, Room 2003, Boston, Mass.
October 13, 1978, 10 a.m. to 3:30 p.m., An-
  napolis  Hilton,  Compromise   and   St.
  Mary's Streets, Annapolis, Md.
October 24, 1978, 9 a.m. to 3 p.m., EPA Re-
  gional Office, 1201 Elm Street, First Inter-
  national Building, 28th Floor, Dallas, Tex.

  Oral  or  written comments  may  be
submitted at  the public hearing and
meetings. Requests  to participate in
the publil* hearing should be directed
to Ms. Gerri Wyer, Public Participa-
tion  Officer,  Office  of  Solid Waste
(WH-562), U.S. Environmental Protec-
tion Agency, 401 M Street SW., Wash-
ington, D.C.  20460. Persons interested
in attending only the public meetings
need  not make a request to partici-
pate.

FOR    FURTHER   INFORMATION
CONTACT:  Mr. George  Garland  at
the above address, 202-755-9125. The
official record  of rulemaking (docket
4002(b)) is located in Room 2107, EPA
(WH-564), 401 M Street  SW., Wash-
ington, D.C. 20460, and is available for
viewing  9 a.m.  to   4 p.m.,  Monday
through  Friday, excluding holidays.
All comments received will be filed in
try's docket.
SUPPLEMENTARY INFORMATION:

      OBJECTIVES OF THE ACT AND
    REQUIREMENTS FOR STATE PLANS

  The objectives of the Act are to pro-
mote  the protection of health and the
environment and to conserve valuable
material  and  energy resources.   In
order to accomplish this, the Act sets
forth a national program to improve
solid   waste  management,  including
control of hazardous  wastes,  resource
conservation,  resource recovery, and
establishment   of    environmentally
sound disposal practices.  This is to be
carried  out  through  a  cooperative
effort among Federal, State,  and sub-
state  governments  and private enter-
prise.
  The' broad scope of this program is
exemplified  by  the  definitions  of
"solid  was^e,"  "solid waste  manage-
ment," and "disposal" in section 1004
of the Act:
  Solid waste:  Any garbage, refuse, sludge
from a waste treatment plant, water supply
treatment plant, or air pollution control fa-
cility and other discarded material, includ-
ing solid, liquid, semisolid, or contained gas-
eous material  resulting  from industrial,
commercial, mining, and agricultural oper-
ations, and from community activities, but
does not include solid or dissolved material
in domestic sewage, or solid or dissolved ma-
terials in irrigation return flows or industri-
al discharges which are point sources sub-
ject to permits under section 402 of the Fed-
eral Water Pollution Control Act, as amend-
ed (86 Stat. 880), or source, special nuclear,
or byproduct  material as defined by the
Atomic Energy Act of 1954, as amended (68
Stat. 923).
  Solid waste management: "The systematic
administration of activities which  provide
for the collection, source separation, stor-
age,  transportation,   transfer,  processing,
treatment, and disposal of solid waste, in-
cluding planning and  management respect-
ing resource recovery and resource conser-
vation.
  Disposal: The discharge,  deposit,  injec-
tion, dumping, spilling, leaking, or placing
of any solid waste or  hazardous waste into
or on any  land or water so that such solid
waste or hazardous waste or any constituent
thereof may enter the environment  or be
emitted into the air or discharged into any
waters including ground waters.
  Section 4002(b) requires the Admin-
istrator to promulgate guidelines for
the development and implementation
of  State  solid  waste  management
plans. States are eligible for financial
assistance under  subtitle D  if  the
State plan has been approved by EPA.
Section 4003 establishes the minimum
requirements  for  approval of  State
plans. These requirements include: (1)
The identification of the responsibil-
ities of State,  local, and  regional au-
thorities  in the development and im-
plementation of the State plan; (2) the
prohibition  of new open  dumps, and
the requirement that all solid waste be
utilized for resource  recovery or dis-'
posed of in an environmentally sound
manner; (3) the closing or upgrading
of existing open dumps; (4) the estab-
lishment  of  State  regulatory powers
necessary  to  implement  the  State
plan; (5)  the elimination of State or
local  prohibitions  of  long-term  con-
tracts for the supply of solid waste to
resource recovery facilities; and (6) the
provision of resource conservation, re-
source recovery,  or  environmentally
sound disposal practices.
  Regulations   to   be   promulgated
under sections 4004 and 1008(a)(3) will
provide  criteria  to  be used  by  the
States in defining  those solid waste
disposal practices that constitute  open
dumping  and  are  to be prohibited
under the State plan according to sec-
tions 4003 (2) and (3). Section 4005(b)
requires  EPA to publish an inventory
of all disposal facilities in the United
States which are open dumps  within
the  meaning  of   the  Act.  Section
4005(c)  provides   that  any  facility
listed  in  the inventory  as  an  open
dump must  be  closed or upgraded
within 5 years according to a State-es-
tablished schedule  containing an en-
forceable sequence  of  actions leading
to compliance.
                              FEDERAL REGISTER, VOL. 43, NO. 167—MONDAY. AUGUST 28. 1978

-------
                                                PROPOSED RULES
                                                                     38535
       GUIDELINES ORGANIZATION

  The guidelines contain seven  sub-
 parts  (A-G). Subpart A  presents the
 purpose and scope, of the guidelines
 and the State plan. It also  contains
 the procedures for State adoption and
 revision and  EPA approval  of  the
 State  plan. In  addition,  important
 terms are defined.
  Subparts B, C, D, and E discuss, re-
 spectively,  (1)  the identification of
 State, local, and regional responsibil-
 ities,  (2) the development of the State
 disposal program, (3) the development
 of the State resource conservation and
 recovery  program, and (4)  facility
 planning and development.
  Each of these subparts lists the over-
 all requirements for plan approval,
 which are  based  upon  the  require-
 ments of the Act. The requirements
 sections are followed by a discussion of
 recommended  procedures.  The   re-
 quirements use the term "shall."  The
 recommendations, which  are advisory,
 use the term  "should."  The recom-
 mendations are provided  to assist the
 States in developing and implementing
 the State  plan. Any  process which
 complies  with  the requirements of
 these  guidelines  will be acceptable to
 EPA  for purposes  of approval of the
 State plan.
  Subpart   F   discusses  coordination
 with other  programs. The broad defi-
 nitions of  solid waste  and  disposal
 make  this coordination especially im-
 portant. Subpart P emphasizes coordi-
 nation with  planning for  residuals
 management under section 208 of the
 Clean Water  Act,  as amended  (33
 U.S.C. 1288), with the National Pollut-
 ant Discharge   Elimination  System
 (NPDES),  under section  402  of that
 Act (33 U.S.C. 1342), and with the  sur-
 face  impoundments  assessment  and
 State  underground injection control
 program  under  the  Safe Drinking
 Water Act (42 U.S.C. § 300f et seq.).
  Subpart G lists the requirements for
 public participation  in  the  develop-
 ment  and implementation of State  and
 substate plans.

        SCOPE OF STATE PLANS

  These  guidelines propose that  the
 State  plan address all solid wastes in
 the State that pose potential adverse.
 effects on  health or the  environment
 or  provide  opportunity for resource
 conservation or  recovery. .The  plan
 should address  residential,  commer-
 cial, and institutional solid waste, haz-
 ardous, industrial, mining, and agricul-
 tural  wates, waste water and  treat-
ment  sludges, septic tank pumpings,
and other pollution control residues. It
should explore the nature and severity
of these categories of solid wastes  and
establish priorities for their manage-
ment.
  The  State plan should  set  forth
planning and implementation activi-
 ties to be carried out by State and sub-
 state agencies.
  Planning.  Planning  is  defined  in
 these  guidelines  as the  process  of
 "identifying problems, defining objec-
 tives, collecting information, analyzing
 alternatives, and determining the nec-
 essary   activities   and   courses   of
 action."  The includes analysis of solid
 waste generation rates and assessment
 of  the adequacy of existing resource
 recovery and disposal facilities and the
 need for new or expanded facilities. It
 also includes  setting priorities for the
 management of different wastes, iden-
 tifying responsibilities, developing the
 necessary  legislation and  administra-
 tive powers to implement  the  plan,
 and planning for State  resource  con-
 servation,  recovery, and disposal  pro-
 grams.
  Many  of these  planning activities
 will be carried out by State agencies.
 However, substate  agencies may need
 to  conduct specific  types of planning
 concerning the number and kinds  of
 facilities  needed in particular areas
 and the  different institutions needed
 (e.g.,  solid waste authorities or dis-
 tricts) for  managing solid wastes. Sub-
 state planning may also be  necessary
 for establishing  coordinated manage-
 ment of  different waste streams (e.g.,
 coincineration  of   residential  solid
 waste and  municipal sewage sludge)  or
 for establishing  disposal or  recovery
 facilities for new waste  streams (e.g.,
 industrial pretreatment residues).1
  Substate agencies may need to devel-
 op more  detailed plans for resource re-
 covery and disposal facilities. .These
 could include technology assessments,
 analysis  of markets for  recovered re-
 sources,  economic  feasibility  studies,
 evaluation of alternative sites, geologi-
 cal  and hydrogeological  investigation,
 and  preliminary   engineering   and
 design studies.
  Implementation.  Implementation  is
 defined in  these guidelines as "putting.
 the plan into practice by carrying out
 planned  activities or insuring such ac-
 tivities are carried out." One aspect  of
 plan  implementation is  carrying out
 the necessary regulatory activities  to
 insure that solid wastes are managed
 and disposed  of  in  a manner that  is
 protective of public health and the en-
 vironment.  This includes developing
 health or environmental  standards for
 facilities, assessing and inspecting fa-
 cilities, conducting a permit or regis-
 tration program, and carrying out the
 necessary  enforcement  activities.  For
 the most  part, such programs  have
been conducted by State agencies, al-
 though certain responsibilities (such
 as inspections) are sometimes delegat-
 ed to local public health agencies.
  The State plan will also result in ac-
 tivities to  encourage resource conser-
vation and resource recovery. This will
include activities to eliminate  institu-
 tional  barriers to  recovery facilities
 (such as prohibitions to long-term con-
 tracts for supplying wastes); activities
 to develop markets for recovered ma-
 terials  (such as State procurement of
 products composed  of such materials);
 and other technical assistance, train-
 ing, information development,  and fi-
 nancial assistance activities. Such ac-
 tivities  require  State,  substate, and
 private sector involvement.
   State plan implementation will also
 include actual site preparation and the
 construction and operation- of resource
 recovery  and disposal  facilities.  In
 many parts of the  country, these ser-
 vices are provided entirely by the pri-
 vate sector. However, there are also
 substate  and State agencies that  are
 involved  in aspects of  facility imple-
 mentation.
   Given the broad  scope of the State
 plan and the necessary involvement of
 a number of agencies and parties, it is
 expected that planning and implemen-
 tation  will be  time-phased over  a
 number of years.

 TIME-PHASING OF PLANNING AND IMPLE-
   MENTATION .UNDER THE STATE PLAN;
   PLAN APPROVAL

   These  guidelines  require  that  the
 State plan be developed within  18
 months, that it cover a minimum of a.
 5-year  time  period, and  that  it  be
 adopted by the State. (Comment is in-
 vited on whether State  administrative
 procedures  adequately  address adop-
 tion  procedures  for  State  plans  or
 whether  approval  should  be by  the
 Governor or State legislature.)  The
 State is to review the plan and, where
 necessary,  revise and  readopt it  at
 least every 3 years.  EPA is to approve
 or disapprove State plans and  to pro-
 vide  financial assistance to  States if
 the State plan has been approved, con-
 tinues to be eligible for approval, and
 is being implemented by the State.
   It will be difficult to completely ful-
 fill the requirements of the guidelines
 in the near term, given the broad defi-
 nitions of disposal and solid waste and
 the ambitious goals of  insuring envi-
 ronmentally sound solid waste disposal
 and  encouraging  resource  recovery
 and  conservation.  Time-phasing  in-
 volves setting priorities among waste
 categories and making  decisions con-
 cerning activities within  a  category.
 Time-phasing should  provide for  co-
- ordination of planning, regulatory pro-
 gram implementation, and facility  im-
 plementation.
  These guidelines  require the State
 plan to describe the  activities to be un-
 dertaken  within  the  5-year period.
 Those activities are to be set forth as
 specifically as possible and are to in-
 clude  detailed schedules and  miles-
 tones.
  The overall, goal of the State plan-
 ning  process is  to  address  planning
                             FEDERAL REGISTER, VOL. 43, NO. 167—MONDAY. AUGUST 28, 1978

-------
38536
          PROPOSED RULES
and implementation  activities for  all
waste  categories that pose  potential
adverse effects on health or the envi-
ronment or provide opportunity for re-
source conservation or recovery. How-
ever, the plan may postpone planning
and implementation activities for cer-
tain waste categories due to the need
to focus resources  on higher priority
categories. The  State  should  deter-
mine which waste categories and activ-
ities have high priority based on: The
current level of management, plan-
ning, and implementation within the
State;  the extent of the solid,waste
management  problem;   the  known
health, evnironmental,  and  economic
impacts; and the resources and man-
agement  approaches  available.  The
State plan may  initially concentrate
planning  and implementation activi-
ties on the high priority waste catego-
ries.
  EPA  may  approve a State  plan
which provides for time-phasing of ac-
tivities in this manner, and which pro-
poses less  than  full  development  of
State  planning and  implementation
activities over the 5-year period, pro-
viding  satisfactory  justification is • in-
cluded in the State plan.

       ANNUAL WORK PROGRAM

  The  annual work program, submit-
ted with a State's  application for  fi-
nancial  assistance  under   section
4008(a)(l) of the Act, will  provide a
basis for .determining   whether the
State plan continues to be eligible for
approval and is being implemented  by
the State. The annual work program
(which is described in the grant regu-
lations (40 CFR Part 35)) summarizes
the current year's  program and sets
forth activities for the  coming year.
Each yea,r, a State's priorities and ac-
tivities should be examined to insure
that the program is directed at achiev-
ing the desired health, enviornmental,
and resource conservation results.
  The  annual  work  program repre-
sents a joint  agreement between EPA
and the State and presents a mutually
satisfactory statement  of reasonable
progress in meeting the requirements
of the Act as expressed in these guide-
lines. It represents a State's obligation
incurred by acceptance of financial as-
sistance and must be developed in con-
sultation with  local  elected  officials
and with public participation.
  In order to  demonstrate that the
State plan is  being  implemented,  a
number of items  developed  under the
State plan are to be included by refer-
ence in  the annual work program.
These include substate plans, plans for
the development of facilities, and com-
pliance  schedules  for  upgrading  or
closing open dumps. Such items are to
be  individually listed in the  annual
work program and  be made available
for review by EPA  and  by the public.
  EPA is considering consolidation of
State work program submissions for
various environmental programs into a
single  State/EPA  agreement.  Com-
ment is  invited on the concept of in-
cluding the State solid waste work pro-
gram submission in such a consolidat-
ed agreement.

        FINANCIAL ASSISTANCE

  Sections 4008 and  4009  of  the  Act
provide for financial  assistance under
subtitle  D (funding of  authorized
•State hazardous waste regulatory pro-
grams is provided under subtitle C of
the Act). Section 4008(a)(l) authorizes
financial assistance for the  develop-
ment and  implementation of  State
plans. The Act states that for this pur-
pose, implementation does not include
the  acquisition, leasing, construction
or modification of equipment or facili-
ties, or the acquisition,  leasing, or im-
provement of  land.  Funds appropri-
ated under this section are to  be allot-
ted to the States in proportion -to pop-
ulation  and are to be  distributed by
States to State and substate  agencies
based-upon the responsibilities of the
respective parties.
  Section 4008(aX2) authorizes finan-
cial  assistance to public solid  waste
management agencies and authorities
for  implementation  of  programs to
provide solid  waste management, re-
source recovery and resource conserva-
tion services   and  hazardous  waste
management. This assistance also does
not cover construction, equipment or
land. Assistance  is  authorized  for
items such as facility  planning  and
feasibility  studies,  consultation,  sur-
veys, and analyses, technology assess-
ments,  legal  expenses, construction
feasibility studies, and economic stud-
ies.  These  grants  may be provided
either directly to substate agencies or
through  the  State.  Financial assist-
ance  under  section  4008(a)(2)  may
only be  provided for programs certi-
fied  by the State as consistent with
the State of substate solid waste man-
agement plan.
  Section 4009  authorizes  grants to
certain rural communities based upon
population and income.  Such  funds
may be provided only to communities
that cannot comply with  the open
dumping prohibition and cannot feasi-
bly  be  included in  a  regional solid
waste  management  facility.  These
funds may be used  for construction
and  equipment. Section 4008(e) ;also
authorizes financial assistance for im-
provement, conversion or construction
of disposal facilities  for communities
having  disposal  facilities  in which
more than 75  percent  of the solid
waste disposal is from areas outside of
the  jurisdiction  of  the  community.
The Act  limits the  latter assistance
program to not more than one commu-
nity in every State.
  In summary, the Act authorizes fi-
nancial assistance for public agencies
to improve  the management  of solid
wastes through the development and
implementation of programs to  regu-
late  solid waste disposal  and hazard-
ous  waste management, programs to
encourage resource recovery and con-
servation, and programs  to plan for
solid waste  processing, disposal or re-
covery facilities. Except for a  limited
number of communities and in special
circumstances, the Act does not autho-
rize  financial  assistance for construc-
tion  and equipment. There  are no
funds  authorized  for acquisition of
land or for  the operation or mainte-
nance  of facilities. These costs  will
have to be borne directly by State and
substate governments and  by  solid
waste generators and facility users.

       OTHER IMPORTANT ISSUES

  There  are a number of important
issues raised by these proposed guide-
lines that require further elaboration
and  explanation.  These   issues,  dis:
cussed below,  are the open dump in-
ventory, abandoned sites, State,  and
substate agency roles  in facility  plan-
ning and' implementation, hazardous
waste management and resource con-
servation and recovery.

 THE OPEN DUMP INVENTORY AS PART OF
           THE STATE PLAN

  These  guidelines require the State
plan to provide for the classification of
disposal facilities according to the cri-
teria for classification of  solid waste
disposal facilities (the criteria; 40 CFR
Part 257) and provide this information
to EPA for  publication "in  the inven-
tory of'open  dumps.  Section 4005(b)
requires EPA  to publish an inventory
of disposal  facilities  that are  open
dumps but does not specify who is to
conduct  the analysis, evaluation and
classification of facilities for that'pur-
pose.  However,   section   1008(a)(3)
states that the criteria are to be used
by the States to define practices which
constitute  open  dumping.  Further-
more, section 4003 requires State plans
to provide for  the closing or upgrading
of open dumps  under  the  require-
ments  of 4005. Therefore, in order for
States  to comply  with the minimum
requirements for State- plan approval,
they must classify facilities in accord-
ance with the  criteria. Such classifica-
tions are a necessary precursor  to
State compliance schedules • and other
enforcement activities. The grant reg-
ulations (40  CFR Part 35) provide for
financial assistance of up  to 100 per-
cent of the allowable  costs of conduct-
ing the inventory of open dumps.
  Since the  listing of a facility in the
open dump  inventory will mean that
the  facility  is in violation of Federal
criteria, adequate evidence, documen-
tation, and due process are necessary.
                             FEDERAL REGISTER, VOL 43, NO. 167—MONDAY, AUGUST 28,  1978

-------
                                                PROPOSED .RULES
                                                                     38537
Therefore, EPA will develop guidance
for conducting facility classifications.
This guidance will attempt to  utilize
existing  State regulatory  approaches
and inspection  procedures whenever
feasible.
  While  the Act calls for  publication
of  the inventory within 1 year, the
complexity of the effort and the time
required to carry it out make it neces-
sary to time-phase the classification of
facilities and the publication of the in-
ventory.   These  guidelines  establish
procedures for such phasing. The clas-
sification of facilities should be coordi-
nated with the development of regula-
tory powers needed for taking enforce-
ment actions and with the  facility
planning needed for replacement  ca-
pacity for open dumps. The State plan
should provide for time-phasing of fa-
cility classifications in a manner so as
to  assert State  control  over all solid
wastes and  disposal categories within
the shortest-practicable time, and in a
manner which provides for health and
environmental protection.

         ABANDONED FACILITIES

  Abandoned, inactive disposal facili-
ties have caused significant  adverse
health   and  environmental   effects.
Therefore, these guidelines state that
abandoned facilities that continue to
produce  such effects  are subject to
classification as open dumps and pub-
lication  in the  inventory. The State
plan need not provide  for statewide
surveillance and  monitoring to deter-
mine locations of all abandoned facili-
ties; rather  the  investigation of aban-
doned facilities should be  directed at
those sites with  a high potential  for
causing severe health  or environmen-
tal problems, such  as leachate con-
tamination of drinking water supplies
and explosions for accumulated gases.
  It is recognized that it may be very
difficult  to  take enforcement  action
with respect  to  abandoned facilities
because  ownership  may  have  been
transferred  or relinquished, and legal
liability  and  financial  responsibility
may be  difficult to establish.  There-
fore, if corrective actions by  facility
owners or operators cannot be brought
about, public agencies  should take the
necessary measures to protect  public
health and  safety.  This  should  in-
clude, as a  minimum, notification of
adjacent residents and other affected
parties of the potential health or envi-
ronmental hazards.
  Recognizing the difficulties  of cor-
recting or upgrading abandoned facili-
ties, preventive measures should  be
taken before facilities become inactive.
The guidelines require the State plan
to provide for facility closure  proce-
dures to  eliminate or minimize adverse
health or environmental effects. Fa-
cility owners  or  operators should  be
required  to  comply with such  proce-
dures through the facility permit or
registration.

STATE AND  SUBSTATE AGENCY RESPONSI-
  BILITIES FOR  FACILITY PLANNING AND
  IMPLEMENTATION

  These  guidelines  require that the
State plan  provide for adequate  re-
source recovery and disposal facilities
and practices necessary to use or dis-
pose of solid waste in an environmen-
tally  sound manner. These guidlines
also recommend a number of  actions
that  could  be undertaken to  help
assure that the necessary facilities and
services are in fact provided for.
  In complying with this requirement,
it is important to strike an appropriate
balance  between  public  and  private
sector activities. These guidelines do
not favor one over the other. In some
parts of the country, private sector ini-
tiatives may be sufficient to insure
that the needed facilities are available.
However, in  other  instances,  there
may be a need for greater involvement
of State or substate governments. This
involvement should include an aware-
ness  of  private sector  activities in
order to  determine  whether public
sector involvement in facility planning
and implementation is necessary.
  EPA recognizes that there is an es-
tablished solid  waste management in-
dustry offering a wide range  of ser-
vices, including the design, construc-
tion,  and operation  of  processing,
treatment, transport, disposal,  and re-
covery facilities. It is not the intent of
these guidelines that the public sector
needlessly supplant or duplicate activi-
ties of the  private sector.  State and
substate agencies  are encouraged to
establish policies for free and unres-
tricted movement of solid waste across
jurisdictional  boundaries  and proce-
dures for sharing  information useful
to prospective  and established entre-
preneurs, as well as to provide relevant
planning information  to  industry re-
garding population and waste  genera-
tion trends, environmental conditions
and other topics that would assist in
the establishment  of  financially and
environmentally sound facilities.
  The. guidelines recommend a state-
wide  assessment of the adequacy of
existing facilities and .an evaluation of
the need for new or expanded facili-
ties. The guidelines purposely leave it
up  to State discretion whether this
needs assessment is to be conducted by
State or substate agencies or by a com-
bination of the two. Where facilities
and practices are  found to be  inad-
equate,  actions should  be taken to
help insure that needed facilities are
developed by State or substate  agen-
cies or by the private sector. For areas
found to have  5 or fewer years of ca-
pacity remaining, more detailed  plan-
ning should be carried out, including
evaluation of technologies and site lo-
cations.   Implementation  schedules
also should be developed.
  Where there  is less  than 2  years'
projected capacity, the 'State should
have the authority to acquire facilities
or cause facilities to be acquired. It is
recognized that  facility acquisition ac-
tivities have,traditionally been theNre-
sponsibility  of regional and local gov-
ernments. However, recent experience
indicates that it is becoming more and
more  difficult  for  substate  govern-
ments to obtain sites for solid waste
disposal  facilities. This  is  especially
true for  facilities that store, treat, or
dispose  of  hazardous wastes. There-
fore, it is important for the State plan
to  explore  options  for  more  direct
State control over siting and facility
development if  local  government and
private sector initiatives fail.  EPA in-
vites  comment  on methods  for  the
State to obtain greater control aver fa-
cility  acquisition; such methods could
include   obtaining the  authority  to
override  local zoning laws or to con-
tract  directly for facilities  and  ser-
vices, requiring facility permits to con-
form  . to regional  plans 'developed
under the State plan, or instituting a
public utility agency to  regulate  the
supply of services.

    HAZARDOUS WASTE MANAGEMENT

  Subtitle C of the Act  provides  foi
the authorization of State programs
for regulating hazardous waste  man
agement and for financial  assistance
for such programs. Guidelines for  the
development and implementation ol
hazardous waste programs  are to b«
promulgated under section 3006 of  th<
Act.  Therefore, the guidelines pro
posed in this rulemaking defer to  the
section 3006 guidelines for the require
ments for authorized State hazardous
waste regulatory programs. However
there are  a number  of hazardous
waste management activities that  an
not regulatory in nature and, thus,  no
covered by the section 3006 guidelines
Such  activities  are to be carried  ou
under the authorities of subtitle D an<
are, subject  to   these  guidelines  fo
State plans. In general, the State plai
is to  describe how hazardous waste
will be managed in the State includinj
identification of responsibilities  fo
that  management and provision  o
necessary hazardous waste treatment
storage, and disposal facilities.
  With regard to hazardous waste fs
cility  planning,  there are certain spt
cial factors to be considered. Most ha:
ardous   waste   recovery,  treatment
storage, and disposal  facilities are pr
vately operated. Hazardous waste ger
erators are often large industries wit
heavy capital investments in plant an
equipment into  which  onsite hazarc
ous waste management facilities hav
been integrated. In addition, there  ai
over  100 private  offsite hazardov
                              FEDERAL REGISTER, VOL. 43, NO. 167—MONDAY, AUGUST 28, 1978

-------
  38538
                                                 PROPOSED RULES
 waste  management  facilities  which
 provide service to many industries.
   The  State  plan should provide' for
 adequate  hazardous  waste recovery,
 treatment, storage, and disposal facili-
 ties, including public facilities where
 necessary.  States  should  develop im-
 plementation  schedules  which  will
 insure  siting  of the necessary hazard-
 ous  waste   management   facilities
 within the State borders. State plans
 should  also  encourage   waste   ex-
 changes  and  other waste utilization
 practices for hazardous wastes.

  RESOURCE CONSERVATION AND RECOVERY

   One  of the  major objectives of the
 Act is  to encourage resource recovery
 and  resource  conservation.  These
 terms  are  defined  in the Act  as fol-
 lows:
   Resource recovery: The recovery of mate-
 rial an'd energy from solid waste.
   Resource conservation: The reduction of
 the amounts of solid waste that are generat-
 ed, ' the reduction  of  overall  resource con-
 sumption, and the  utilization of recovered
 resources.
 These  guidelines establish several re-
 quirements for  State1 plans directed
 toward achieving this objective.
   The  guidelines  require the  State
 plan to provide for the development of
 a policy and strategy  to encourage re-
 source  recovery and resource conserva-
 tion. This strategy should focus on re-
 moving existing  technical,  economic,
 and  institutional  constraints  that
 impede increased  resource  recovery
 and  conservation. State  activities  in
 this  area could  include technical as-
 sistance,  training, information devel-
 opment and  dissemination, financial
 support programs, and programs to de-
 velop markets for recovered materials
• and energy.
   The  Act  requires  State plans  to
 Insure  that local governments are not
 prohibited  under  State or local law
 from entering into long-term contracts
 for supplying  solid wastes to resource
 recovery  facilities. This  section re-
 flects the  concern that  the develop-
 ment of resource  recovery  facilities
 has been hindered by restrictive pro-
 curement laws. The guidelines  recom-
 mend that the State plan provide for
 State agency  review of pertinent State
 and local statutes, and for  the develop-
 ment of a strategy for eliminating the
 long-term contracting restrictions. It is
 recognized  that States and State agen-
 cies may have limited ability to modify
 local procurement laws. Therefore, co-
 operation of  local governments and
 public  education and participation are
 important  in meeting  this require-
 ment.
   Section  6002  of the Act requires
 State agencies to purchase items  com-
 posed of  the highest percentage of re-
 covered materials  practicable, when-
 ever Federal  funds are used for  such
purchases. Although section 6002 is
entitled  "Federal  Procurement,"  the
requirement in section 6002(c) applies
to State procuring agencies by virtue
of  definition  (17)  in  section  1004.
These guidelines allow States to delay
in  complying  with  the requirement
until  EPA issues additional guidelines
under section  6002(e)  which will  rec-
ommend procedures for purchasing re-
covered materials  and  provide  infor-
mation on their availability and uses.
These guidelines also recommend that
the State plan provide for the develop-
ment  of a policy to encourage procure-
ment  of recovered materials and exam-
ination of potential  uses of recovered
materials by State  purchasing  agen-
cies.
  It is  recognized  that  State  solid
waste management agencies are gener-
ally not involved in procurement prac-
tices and policies. Therefore, the State
plan should identify the agencies with
responsibility in this area and provide
for the   necessary  actions  by  such
agencies  in order to meet this require-
ment.
  The guidelines recommend resource
recovery and resource  conservation as
the preferred  methods of  solid  waste
management   whenever   technically
and economically  feasible.  While re-
source recovery and  conservation may
reduce land disposal needs,  however,
these  methods will not eliminate  the
need  for land  disposal. It is expected
that in  the near future, resource re-
covery and conservation will have only
a limited impact  on the solid  waste
generated   nationwide.   Therefore,
there  will continue to be a need for en-
vironmentally  sound land disposal fa-
cilities in order to  meet the objectives
of the Act.

   COORDINATION WITH OTHER ACTS,
    GUIDELINES, AND REGULATIONS
  These  guidelines should be consid-
ered along with certain other guide-
lines and regulations being promulgat-
ed under the Act and  with the provi-
sions of several other Acts.

  COORDINATION WITH WATER QUALITY
        MANAGEMENT AGENCIES

  Subpart F  of these  guidelines  ad-
dresses  the  requirements  for coordi-
nating the State plan with programs
under section  208 of the Clean Water
Act, as amended (33  U.S.C. 1288). Sec-
tion 208 provides for the identification
of  complex  water  quality  problem
areas  and  for the  designation  of
areawide  agencies in  those  areas to
conduct  water  quality  management
planning. The State is responsible for
such planning in all areas of the State
for which an areawide agency has not
been identified and for coordination of
all  water quality management activi-
ties within the State.  As part of  this
effort, State and areawide agencies are
to identify a process to control the dis-
position  of  all residual  (solid)  waste
which  affects  water  quality.  After
completion of such planning, the Gov-
ernor is to designate agencies to imple-
ment various elements of the plan.
  Subpart F discusses the need to con-
sider water quality management agen-
cies  when making agency  identifica-
tions for solid waste planning and im-
plementation. It  also  discusses  the
need to  establish  coordination proce-
dures when separate agencies are iden-
tified. The following types of coordina-
tion should take place:
  1. Use  of a common data base (e.g.
demographic and   population projec-
tions and geographic boundaries);
  2. Use of compatible  report formats,
maps, scales, legends, and so forth;
  3. Formulation of consistent policies
for a  sludge and  residuals manage-
ment;
  4.  Coordinated   identification  of
State legislative changes needed for
implementation; and
  5. Coordination of program develop-
ment, implementation  strategies,  and
public participation programs.

     COORDINATION WITH SURFACE
        IMPOUNDMENT STUDIES

  Section 1442(a)(8)(C)  of  the  Safe
Drinking  Water  Act,"  as   amended
(SDWA)  (42  U.S.C. 300J-1)  requires a
study of  the  nature and  extent of the
impact   on   underground  water  of
ponds,  pools, lagoons, pits,  or  other
surface disposal of contaminants in
underground water recharge areas. In
partial fulfillment  of this requirement,
EPA  intends  to   conduct,  through
grants  to State agencies, an  assess-
ment of  surface  impoundments  and
their effects on ground water.
  There is the potential  for confusion
and duplication of effort between the
studies of surface impoundments to be
conducted under the SDWA and the
inventory of open dumps to be con-
ducted under the Solid Waste Disposal
Act. Therefore, the State financial as-
sistance  programs under both  Acts
must be closely coordinated. The stud-
ies and assessments planned under the
SDWA should be used  as the basis for
identifying  those   surface  impound-
ments that have thejjreatest potential
for adverse effects and should be used
by the States in developing the open
dump inventory. Those impoundments
which  are identified  as having  the
greatest  potential   for  serious  impact
on  ground  water   quality should be
considered high priority for develop-
ment of the inventory. Such impound-
ments  which are found to violate the
criteria should be  listed  in  the  inven-
tory and  be  liable for closure or up-
grading.  Those surface impoundments
that receive hazardous wastes are sub-
ject  to the regulations for  hazardous
                              FEDERAL REGISTER, VOL. 43, NO.  167—MONDAY, AUGUST 28, 1978

-------
                                                 PROPOSED RULES
                                                                                                             38539
waste  disposal  facilities  promulgated
under subtitle C of the Act.
  While the  inventory  process and
subtitle C  regulations will begin  to
bring such facilities  under State cop-
trol under  the Solid Waste Disposal
Act, EPA has not  yet determined the
best regulatory approach to the con-
trol of  surface impoundments.  EPA
will continue  to  explore and  reeval-
uate its authorities  under  the Solid
Waste Disposal Act, the Safe Drinking
Water Act, the Clean Water Act, and
the Toxic  Substances Control Act (15
U.S.C. 2601 et seq.) in order to deter-
mine the  best  regulatory  approach
under  any or a combination of these
various  authorities. If these authori-
ties are not sufficient to assure the
•adequate control  of  the disposal  of
wastes   through   surface   impound-
ments,  EPA will seek additional legis-
lative authority. States and the gener-
al public will be allowed  ample oppor-
tunity to comment on the most effec-
tive means of  regulating surface im-
poundments such  as pits, ponds, arid
lagoons.

COORDINATION WITH THE NATIONAL POL-
  LUTANT   DISCHARGE   ELIMINATION
  SYSTEM (NPDES)

  Section 402 of the Clean Water Act,
as amended (33 U.S.C. 1342) describes
the National  Pollutant   Discharge
Elimination System (NPDES) govern-
ing discharge of pollutants  into navi-
gable waters. Permits issued under sec-
tion 402 should be coordinated  with
hazardous  waste and solid waste man-
agement permits,  where  applicable.
The following aspects of the NPDES
system  should be taken into account:
  1. State  or  Federal  issuance  of
NPDES permits for facilities disposing
or  utilizing municipal   waste   water
treatment  sludge, including new facili-
ty  permits  and compliance  schedules
under existing permits.
  2. State  or  Federal  issuance  of
NPDES permits for facilities disposing
or utilizing industrial pollution control
sludges, including hew and existing fa-
cilities.
  3. State  or  Federal supervision  of
pretreatment  programs  requiring fa-
cilities  to  comply  with  requirements
and compliance schedules before dis-
charging into  municipal sewer sys-
tems.

     COORDINATION WITH  MINING
         REGULATORY AGENCIES

  Title  IV of the Surface Mining Con-
trol and Reclamation Act of 1977 (30
U.S.C.  1231) provides for the establish-
ment of a fund  for reclamation  of
abandoned mining lands. To be eligi-
ble  to   receive this  funding,  States
must first  develop  an  enforcement
program for wastes from  active mines,
subject to Department of the Interior
and EPA approval (title  V). All mine
wastes must be disposed in accordance'
with performance standards to be pro-
mulgated by  the  Office  of Surface
Mining,  Department of the  Interior.
Coordination between these EPA and
Department of the Interior  programs
will facilitate the inventory of mining
wastes and may increase the beneficial
use of sludge as a soil conditioner in
reclamation of abandoned lands.

 COORDINATION WITH OTHER GUIDELINES
           AND REGULATIONS '
  Other guidelines and regulations de-
veloped under the  Act which should
be  considered  in  conjunction  with
these  guidelines ^tor State  plans in-
clude:
  1. Interim regulations to implement
the Resource Conservation and Recov-
ery Act  of 1976 (40 CFR  Part 35).
These  regulations establish procedures
and policies  for  grants and financial
assistance programs.
  2. Identification of regions and agen-
cies for solid waste management,  Inter-
im  guidelines  (40 CFR  Part  255).
These  guidelines present criteria and
procedures for identification of region-
al boundaries and responsible agencies
for solid  waste  planning  and imple-
mentation.
  3. Proposed  regulations for public
participation (40  CFR Part 25). Sec-
tion 7004(b) of the Act requires EPA
and the States to provide for, encour-
age, and assist public participation in
the" development, revision, implemen-
tation, or enforcement of  any regula-
tion, guideline,  information, or pro-
gram   under  the  Act. The current
guidelines  for public participation in
solid waste management (40 CFR Part
249) will be superseded by a new EPA
regulation, to be codified  as 40 CFR
Part 25. The proposed part 25 cpntains
general public participation require-
ments  for programs under the  Solid
Waste  Disposal  Act, as amended by
RCRA, as well as  for  the  programs
under the Clean Water Act, as amend-
ed (33 U.S.C. 1251 et seq.) and the Safe
Drinking Water  Act, as amended (42
U.S.C.  300f et seq.). Since part 25 does
not contain public participation  re-
quirements  .specific to  solid   waste
plans, subpart G  of- this part addresses
public  participation in the  develop-
ment and implementation of State and
substate, plans. Subpart G references
the proposed part  25 requirements. If
part 25 is not promulgated as a final
rule  prior  to this  part 256, part  249
will take  precedence until part  25 is
promulgated.
  4. Solid waste disposal facilities, pro-
posed  criteria  for  classification  (40
CFR Part 257).  This regulation pro-
poses  minimum criteria for determin-
ing which solid waste land disposal fa-
cilities shall be classified as posing no
reasonable probability  of  adverse ef-
fects on health or the environment.
  5. State  hazardous waste programs,
proposed  guidelines  (40  CFR -Part
250).  This rule describes  the various
provisions  and capabilities a State haz-
ardous  waste program must have in
order  to  qualify  for  authorization
under the  Act.  Other regulations for
hazardous  waste  management devel-
oped  under  subtitle  C  of  the  Act
should also be considered.
  6. Resource recovery facility guide-
lines <4D CFR Part 245). These guide-
lines  apply to Federal agencies' plan-
ning and establishment of resburce^re-
covery facilities.

           ECONOMIC IMPACT
  NOTE.—EPA has determined that this doc-
ument does  not require an economic impact
analysis  statement under Executive Order
12044 and OMB Circular A-107.
  Djated: August 23, 1978.
              DOUGLAS M. COSTLE,
                     Administrator.
  Title  40  CFR  is  proposed  to  be
amended to add a new part 256 read-
ing as follows:
PART  256—GUIDELINES  FOR DEVELOPMENT
  AND IMPLEMENTATION OF .STATE SOLID
  WASTE MANAGEMENT PLANS

    Subpart A—Purpose, G«*ral R*auir*rMnt«,
               0»finitioni

Sec.
256.01  Purpose and scope of the guidelines.
256.02  Scope of the State solid waste man-
    agement plan.
2S6.03  State  plan  submission,  'adoption,
    and revision.
256.04  State plan approval, financial assist-
    ance.
256.05  Annual work program.
256.06  Definitions.

    Subpart B—Identification of R«poa»ibilrH*»;
           Di.tribution of Funding
256.10
256.11
Requirements.
Recommendations.
    Subpait C—Solid Watt* Disposal Program*

256.20  Requirements for the State regula-
   tory powers.
256.21  Recommendations for State regula-
   troy powers.
2S6.22  Requirements for closing or upgrad-
   ing open dumps.
256.23  Recommendations for closing or up-
   grading open dumps.
256.24  Requirements to prohibit the estab-
   lishment of new open dumps.

  Subpart D—Reiaurc* Conservation and Rmoure*
            Recovery Programs

256.30  Requirements.
256.31  Recommendations   for  developing
   and Implementing resource conservation
   and recovery programs.

  Subpart E—Facility Planning and Implementation

256.40  Requirements.
256.41  Recommendations for assessing the
   need for resource recovery and disposal
   facilities.
256.42  Recommendations for assuring  fa-
   cility development.
                              FEDERAL REGISTER, VOL. 43, NO. 167—MONDAY, AUGUST 28, 1978

-------
38540
          PROPOSED RULES
Sec.
256.43  Recommendations  for  hazardous
   waste facility planning and  develop-
   ment.
   Subport f—Coordination With Other Programs
256.50  Requirements.
        Support G—Public Participation
256.60*  Requirements for public participa-
   tion in State and substate plans.
256.61  Requirements for public participa-
   tion in the annual State work program.
256.62  Requirements for public (jarticipa-
   tion in State regulatory development.
256.63  Requirements for public participa-
   tion in the permitting of facilities.
  AT/THORITY: Sees. 4002(b) and 4003 of the
Solid Waste Disposal Act, as amended, Pub.
L. 94-580;  90 Stat.  2813, 2814; 42 U.S.C.
6942(b), 6943.  *

  Subpart A—Purpose, General Requirements,
              Definitions
§ 256.01 Purpose and  scope of the guide-
    lines.
  (a) The purpose of these guidelines
is to assist in the development and im-
plementation  of  State  solid waste
management plans, in accordance with
section 4002(b) of the Solid Waste Dis-
posal Act, as amended by the Resource
Conservatign  and  Recovery  Act  of
1976 (42 U.S.C. 6942(b)) (the "Act").
These  guidelines contain methods for
achieving the objectives of envirbmen-
tally sound management and disposal
of solid and hazardous waste, resource
conservation,  and  maximum  utiliza-
tion of valuable resources.
  (b)  These guidelinges address  the
minimum  requirements for approval
of State plans as set forth in section
4003 of the Act. These are:
  (1) The  plan shall identify, in ac-
cordance with section 4006(b), (i)  the
responsibilities of State, local, and re-
gional  authorities in the implementa-
tion of the State plan, (ii) the distribu-
tion of Federal funds to the authori-
ties responsible for development and
implementation of the State plan, and
(iii) the means for coordinating region-
al planning and implementation under
the State plan.
  (2)  The  plan shall, in accordance
with section 4005(c),  prohibit the es-
tablishment  of new  open   dumps
within the State, and contain  require-
ments that all solid waste (including
solid waste originating in other States,
but  not including  hazardous  waste)
shall be (i) utilized for resource recov-
ery or  (ii) disposed of in sanitary land-
fills (within  the meaning of section
4004(a)) or otherwise disposed of in an
environmentally sound manner.
  (3) The  plan shall provide  for  the
closing or  upgrading of  all  existing
open dumps within the State pursuant
to the requirements of section 4005.
  (4) The plan shall provide for the es-
tablishment of  such State regulatory
powers as  may be necessary to imple-
ment the plan.
  (5) The plan shall provide that no
 local  government  within the  State
 shall  be prohibited  under  State or
 local law from entering into long-term
 contracts for the supply of solid waste
 to resource recovery facilities.
•  (6)' The plan  shall  provide for re-
 source conservation or recovery  and
 for the disposal  of solid waste in sani-
 tary  landfills or for any  combination
 of practices so as may be  necessary to
 use that is environmentally sound.
  (c) These guidelines address the re-
 quirement  of section  4005(c) that a
 State.plan:
 shall establish, for any entity which demon-
 strates that it has considered other public
 or private alternatives for solid waste man-
 agement to comply with the prohibition on
 open dumping and is unable to utilize such
 alternatives to so comply, a timetable or
 schedule of compliance for such practice or
 disposal of solid waste which  specifies a
 schedule of remedial measures, including an
 enforceable sequence of actions or oper-
 ations leading to compliance with the prohi-
 bition on open  dumping of solid  waste
 within a  reasonable time (not to exceed 5
 years from the date of publication of the in-
 ventory).
  (d)  These  guidelines also  describe
 certain hazardous waste planning ac-
 tivities not included  in  the section
 3006 guidelines for authorized State
 hazardous waste programs. The  plan-
 ning  activities  described   in  these
 guidelines are to be included in  the
 State plan.

 §256.02  Scope of the State solid  waste
    management plan.
  (aXl)  The  State  plan shall address
 all solid waste in the State that poses
 potential adverse effects on  health or
 the environment or provides opportu-
 nity  for resources conservation  or re-
 source ^recovery. The plan shall consid-
 er:
  (i)  Hazardous wastes; (ii) Residen-
 tial,   commercial,  and  institutional
 solid waste; (iii) Wastewater treatment
 sludge; (iv) Pollution control residuals;
 (v)   Industrial  wastes;  (vi) Mining
 wastes; (vii) Agricultural  wastes; (viii)
 Water  treatment  sludge;   and   (ix)
 Septic tank pumpings.
  (2) The State plan shall consider the
 following aspects of solid waste man-
 agement:
  (i)  Collection;  (ii) Source separation;
 (iii)  Storage; (iv)  Transportation; (v)
 Transfer; (vi) Processing; (vii) Treat-
 ment; (viii) Resource conservation; (ix)
 Resource recovery;  and (x) Disposal.
  (b)  The  State plan  shall establish
 and  justify priorities  and timing for
 actions. These priorities shall be based
 on the  current level  of solid  waste
 management planning  and implemen-
 tation within the State, the extent of
 the solid waste  management problem,
 the  health,  environmental  and  eco-
 nomic impacts  of  this problem,  and
the  resources  and management  ap-
proaches available.
  (c) The State plan shall set forth an
orderly and manageable process  for
achieving the objectives .of the Act  and
meeting the  requirements  of  these
guide- lines. This "process  shall  de-
scribe as specifically as possible ,the ac-
tivities to be undertaken, including de-
tailed schedules and milestones.
  (d)  The  State  plan shall  cover  a
minimum of a 5-year time period from
the date submitted to EPA for approv-
al.
  (e) The State plan shall identify ex-
isting.State legislative authorities for
solid waste management and shall pro-
vide for the identification and acquisi-
tion of additional legislative  authori-
ties  and regulatory,  administrative*-
and judicial powers as may be neces-
sary to meet the requirements of these
guidelines. The plan shall  contain a
schedule for obtaining these  authori-
ties and powers.

§256.03  State plan  submission, adoption,
   and revision.
  (a)  To be considered for approval,
the State plan shall be  submitted to
EPA within 18 months after final pro-
mulgation of these guidelines.
  (b)  Prior to submission to EPA,  the
plan  shall  be  adopted by  the  State
pursuant to State administrative pro-
cedures.
  (c)  The plan shall be  developed in
accord with public participation proce-
dures required by 40 CPR Part 25  and
other guidance for public participation
that may be issued by EPA.
  (d)  The  plan  shall  contain proce-
dures for  revision.  The State plan
shall be revised  by the State, after
notice and public hearings,  when  the
Administrator, by regulation, or  the
State determines, that:
  (1)  The State plan is not  in compli-
ance  with  the requirements of these
guidelines;
  (2)  Information  has become availa-
ble which demonstrates the inadequa-
cy of the plan; or
  (3)  Such revision is-otherwise neces-
sary.
  (e)  The State plan shall be reviewed
by the State and, where necessary, re-
vised and readopted not less frequent-
ly than every 3 years.

§ 256.04  State plan approval, financial as-
    sistance.
  (a) The Administrator shall, within 6
months after a  State plan has been
submitted for approval, approve or dis-
approve the plan. The Administrator
shall approve a plan if he determines
that:'
  (1) It meets the requirements of
these guidelines  which  address  sec-
tions 4Q03 (1), (2), (3), and (5), and
  (2) It contains provisions for revision
pursuant to § 256.03.
                              FEDERAL REGISTER, VOL. 43, NO. 167—MONDAY, AUGUST 28, 1978

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                                                 PROPOSED RULES
                                                                                                           38541
   (b)  The Administrator shall review
 approved plans from time to time, and
 if he  determines that revisions or cor-
 rections are  necessary  to  bring  such
 j>lan  into  compliance with all of the
 requirements of these  guidelines,  in-
 cluding the  requirements  which ad-
 dress  sections 4003 (4) and  (6)  and any
 new  or  revised  requirement estab-
 lished by amendment to this  part, he
 shall  notify the State and  provide an
 opportunity for such revisions  and cor-
 rections and  for an appeal and public
 hearing.  If  the plan  continues  to
 remain out  of compliance, he  shall
 withdraw his approval of such  plan.
   (c)  Such  withdrawal of approval
 shall  cease  to  be  effective upon the
 Administrator's  determination   that
 the State plan complies with the  re-
 quirements of. these guidelines.
   (d) The Administrator shall  approve
 a State application for financial assist-
 ance under subtitle D of the Act, and
 make grants  to such State, if  the Ad-
 ministrator determines  that the State
 plan  continues to be eligible  for ap-
 proval and  is being implemented  by
 the State.
   (e) Upon withdrawal of approval of a
 State  plan,  the  Administrator  shall
 withhold Federal financial  and techni-
 cal  assistance under subtitle D (other
 than such technical assistance as may
 be necessary to assist in obtaining re-
 instatement  of approval)  until  such
 time as approval is  reinstated. (Proce-
 dures for termination of financial  as-
 sistance and for settlement  of  disputes
 are  contained in 40 CPR 30, appendix
 A, articles 7 and 8.)

 § 256.05  Annual work program.
   (a)  The  annual work program sub-
 mitted for  financial assistance under
 section 4008(a)(l) and described in the
 grant  regulations  (40  CFB Part 35)
 shall be reviewed by the Administrator
Mn order to  determine whether  the
 State  plan is being implemented  by
 the  State.
  (b) The Administrator and the State
 shall  agree  on the contents  of  the
 annual work program.  The Adminis-
 trator will  consider State initiatives
 and priorities, in light of the  goals of
 the  Act, in determining annual work
 programs for each State. The annual
 work program represents a  State's ob-
 ligation incurred by acceptance  of fi-
 nancial assistance.
  (c) Annual guidance for the develop-
 ment  of State work  programs will be
 issued by  EPA. While  this guidance
 will establish annual national prior-
 ities,  flexibility will be provided  in
 order  to accommodate differing State
 priorities,
  (d)  The following items developed
 under the "State plan shall be included
 by reference  in the annual work pro-
 gram:
  (1) Substate, regional, and local solid
waste management plans,
  (2) Plans for the development of fa-
cilities and services, including hazard-
ous waste management  facilities  and
services,
  (3)  Compliance schedules  for  up-
grading or closing open  dumps neces-
sary to meet- the requirements of sec-
tions 4003(3) and 4005(c).
  (e) The annual work program shall
itemize the  distribution  of  Federal
funds  to  agencies responsible for the
development  and implementation of
the State  plan.

§ 256.06  Definitions.
  Terms not defined below have  the
meanings assigned  them  by section
1004 of the Act.
  "Abandoned facility" means an inac-
tive solid  waste disposal  facility which
poses a reasonable probability of ad-
verse effects on health or the environ-
ment.
  "The Act" means the Solid Waste
Disposal Act,  as  amended  by the Re-
source Conservation and Recovery Act
of 1976 (42 U.S.C. 6901 et seq.).
  "Closed facility"  means a facility
which  has been properly closed so as
to eliminate or minimize  adverse  ef-
fects on health or the environment.
  "Criteria" means  the  "Criteria for
Classification  of Solid Waste Disposal
Facilities," 40 CFR  part 257, promul-
gated under section 4004(a) of the Act.
  "Facility" refers  to a solid  waste
proc- essing or disposal facility or a re-
source recovery facility, including land
used for  solid waste disposal within
the meaning of the  Act. Examples in-
clude  sanitary landfills, surface  im-
poundments,   landspreading   oper-
ations, incinerators,  transfer stations,
pyrolysis plants, refuse fired boilers, et
cetera.
  "Implementation"   means  putting
the plan into practice by carrying out
planned  activities, including compli-
ance and enforcement activities, or in-
suring  such activities are carried out.
  "Inventory of  open  dumps" means
the inventory required under section
4005(b) and is defined as the list pub-
lished by EPA of those disposal facili-
ties which do not meet the criteria.
  "Operator" includes facility owners
and operators.
  A "permit" is an entitlement to com-
mence  and continue  operation of a fa-
cility as long  as  both pr6cedural and
performance standards are met. The
term "permit" includes any functional
equivalent such as a registration or li-
cense.
  "Planning"   includes    identifying
problems,  defining objectives, collect-
ing information, analyzing alternatives
and determining necessary activities
and courses of action.
  "Provide for"  in  the  phrase "the
plan shall (should) provide for" means
explain, establish or set forth steps or
courses of action.
  The term  "shall"  denotes require-
ments for the development and imple-
mentation of the State plan.
  The term "should" denotes recom-
mendations for the development and
implementation of the State plan.
  "Substate" refers to any public re-
gional, local, county, municipal, or in-
termunicipal  agency,  or regional or
local public (including interstate) solid
or hazardous waste management au-
thority, or other public  agency below
the State level.

 Subpart B—Identification of Responsibilities;
         Distribution of Funding

§ 256.10  Requirements.
  (a)   In   accordance with   sections
4003(1) and  4006  and the guidelines
for identification of regions and agen-
cies  for solid waste management (40
CFR  Part  255), the  State plan shall
provide for:
  (1) The identification of the respon-
sibilities of State and substate (regio.n-
al, local and interstate) authorities in
the development and  implementation
of the State plan;
  (2) The means of distribution of Fed-
eral funds to the authorities responsi-
ble for development and implementa-
tion of the  State plan; and
  (3) The means for coordinating sub-
state planning and implementation.
  (b)  Responsibilities shall be identi-
fied  for the  classification of disposal
facilities for  the  inventory   of  open
dumps.
  (c)  Responsibilities shall be identi-
fied for development and implementa-
tion of the State regulatory program
describes in subpart C of this  part.
  (d)  Responsibilities shall be identi-
fied  for the  development and imple-
mentation  of  the State resource con-
servation and resource recovery  pro-
gram described  in Subpart D of this
part.
  (e) State, substate and private sector
responsibilities shall be identified for
the planning  and implementation of
solid  and  hazardous  waste  manage-
ment facilities and services.
  (f)  Financial  assistance under  sec-
tion  4Q08(a)(l)  shall be  allocated by
the State to  State  and  substate au-
thorities  carrying  out planning  and
implementation of  the   State  plan.
Such  allocation  shall be  based on the
responsibilities of  the respective  par-
ties   as  determined  under   section
4006(b).

§ 256.11 Recommendations.
 (a) Responsibilities should be identi-
fied for each of the solid waste types
listed in §256.02(a)(l).  ,
 (b) Responsibilities should be identi-
fied for each  of the aspects of solid
                              FEDERAL REGISTER, VOL. 43, NO. 167—MONDAY, AUGUST 28, 1978

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38542
          PROPOSED RULES
waste management  listed in § 256.02
  (c) Responsibilities should be identi-
fied for planning and designation  of
ground water  use  as provided for  in
the  criteria for classification of solid
waste disposal facilities (40 CFR Part
257) and for  assessing other factors
critical to Criteria classifications.
  (d) Responsibilities should be identi-
fied for the development and imple-
mentation  of  the  authorized State
hazardous  waste  management  pro-
gram under subtitle C of the Act.
  (e) The State plan should include a
schedule  and procedure  for the  con-
tinuing review, reassessment and reas-
signment of responsibilities.

  Subpart C — Solid Waste Disposal Programs

  NOTE.— This Subpart  addresses  the  re-
quirements contained in sections 4003 (2),
(3)  and (4)  of  the Act. Section 4003(4),
which covers the establishment of State reg-
ulatory powers necessary to  implement the
plan, is addressed first. The requirement of
section 4003(3),  that  the plan provide for
the closing or upgrading of open dumps, is
addressed as one application of those regu-
latory powers. The requirement in section
4003(2),  that the plan  prohibit the estab-
lishment of new open dumps, is addressed as
the second application of those powers.

§ 256.20  Requirements  for the State regu-
    latory powers.
  The State plan shall provide for the
establishment  of such State  regula-
tory powers as may be  necessary  to
prohibit new open dumps and close  or
upgrade  all  existing open  dumps.
These regulatory powers:
  (a) Shall be based on solid waste dis-
posal standards which are equivalent
to or more stringent  than the criteria
for classification of solid waste dispos-
al facilities (40 CFR Part 257). Such
standards   shall   be   determinate,
achievable  and enforceable^ and  the
methodology for establishing  compli-
ance shall be specified.
  (b) Shall -include surveillance capa-
bilities  necessary to detect adverse en-
vironmental effects from solid waste
disposal facilities.  Such  capabilities
shall include access for inspection and
monitoring by  regulatory officials and
the  authority to  establish operator
monitoring   and  reporting  require-
ments.
  (c) Shall  utilize  assessment  proce-
dures for the  evaluation  of facilities
which  compare the surveillance find-
ings to  the standards, note all discrep-
ancies,  and prescribe satisfactory re-
medial measures.
  (d) Shall  make use of a permit  or
registration  program  which  ensures
that the  establishment of new open
dumps is prohibited.
  (e) Shall have administrative and ju-
dicial enforcement capabilities, includ-
ing enforceable orders, fines and other
administrative procedures, as  neces-
sary to achieve compliance with stand-
ards including closure or upgrading of
all open dumps. The enforcement ca-
pabilities shall insure expeditious clo-
sure or upgrading of the facilities in a
manner  so  as to minimize or bring
under control  adverse environmental
or health effects.

§ 256.21  Recommendations for State regu-
   latory powers.
  The following are recommendations
for State regulatory powers as may be
necessary to prohibit new open dumps
and close or upgrade all existing open
dumps.
  (a) Solid waste disposal standards:
  (1) Should be based on the health
and environmental impacts of disposal
facilities.
  (2) Should specify design and oper-
ational standards.
  (3) Should take into account the cli-
matic,  geologic  and  other  relevant
characteristics of the State.
  (b) Surveillance systems  should es-
tablish  monitoring  requirements  for
facilities.
  (1) Every  facility should be evaluat-
ed for potential adverse health and en-
vironmental effects.  Based  on  this
evaluation, instrumentation, sampling,
monitoring,  and  inspection  require-
ments should be established.
  (2) Inspectors should be trained and
provided  detailed  instructions  for
checking on'the procedures and condi-
tions that  are specified in the engi-
neering plan  and site permit.  Provi-
sions should be made to insure chain
of custody for evidence.
  (c) Facility assessment and prescrip-
tion  of  remedial measures should be
carried out by adequately  trained or
experienced professional staff, includ-
ing engineers and geologists.
  (d) The State permit system should
provide  the administrative control to
prohibit  the  establishment  of  new
open dumps and to assist in meeting
the requirement  that all  wastes be
used or disposed in an environmental-
ly sound manner.
  (1) Permitting procedures  for  new
facilities should require applicants to
demonstrate  that the facility  will
comply with the criteria.
  (2) The permit system should speci-
fy, for the facility operator, the loca-
tion, design, construction, operational,
monitoring, reporting, completion and
maintenance requirements.
  (3) Administrative procedures should
be adequate for assuring due process
of  law  and  withstanding  judicial
review.
  (4) Permits should only be issued to
facilities that are consistent with the
State plan,  or with substate plans de-
veloped under the State plan.
  (e) The enforcement system should
provide   both  administrative  proce-
dures and judicial remedies to enforce
the prohibition of open dumping and
the compliance schedules and closure
procedures for open dumps.
  (1) Procedures should be established
to facilitate court access, and to obtain
court orders and  other rulings.  Per-
mits,  surveillance, and enforcement
system capabilities should be designed
for supporting court action.
  (2) Detection capabilities and penal-
ties for false reporting should be pro-
vided for.

§ 256.22  Requirements for closing or up-
   grading open dumps.
  In meeting the requirement of sec-
tion 4003(3) for closing or upgrading
open dumps:
  (a) The State plan shall provide for
the  classification  of  existing  solid
waste disposal  facilities according to
the Criteria. This classification  shall
be submitted to EPA,  and facilities
classified as open dumps shall be pub-
lished in the inventory.
  (b) The classification of  facilities as
open dumps shall be sufficiently docu-
mented to withstand judicial review.
  (c) Each operator shall (1) be  noti-
fied of the State's intent to submit the
name of the facility to EPA for publi-
cation  as an open dump in the inven-
tory, (2) be provided a  summary of the
evidence upon which the classification
is  based, and (3) be provided with an
opportunity to  appeal in  accordance
with State laws and regulations.
  (d) The State plan shall provide that
any facility classified as an open dump
is prohibited except in the case of a fa-
cility under a timetable or schedule of
compliance  as  established  in  para-
graph (e) of this section.
  (e) The State plan shall provide for
the establishement of a procedure by
which  any entity which demonstrates
that it has considered other public or
private alternatives to comply  with
the prohibition on open dumping and
is unable to utilize such alternatives to
so comply, may obtain a timetable or
schedule for compliance which speci-
fies a schedule  of remedial measures,
and  an  enforceable sequence of ac-
tions, leading to compliance within a
reasonable time (not to exceed 5  years
from the date  of  publication of  that
facility in the inventory.)
  (f) The State plan shall  provide for
an orderly time-phasing of the dispos-
al facility classifications described in
paragraph (a) of this section. The de-
termination of  priorities for the classi-
fication  of disposal facilities  shall be
based upon:
  (1) The potential. health and  envi-
ronmental impact of the solid waste or
disposal facility;
  (2) The availability of State regula-
tory and enforcement powers; and
  (3) The availability  of Federal and
State resources for this purpose.
                              FEDERAL REGISTER, VOL 43, NO. 167—MONDAY, AUGUST 28, 1978

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                                                 PROPOSED RULES
                                                                                                            38543
  (g) Each facility classified as an open
dump  shall be  issued a  schedule  for
closure or upgrading which shall be in-
corporated  by   reference  into   the
annual work  program and be made
publicly available. The schedule may
be revised in accord with State proce-
dures and without prior notification of
EPA. Schedule revisions shall be refer-
enced  in subsequent annual work pro-
grams.
  (h) For each open dump to be closed,
the  State plan  shall provide for  clo-
sure procedures to eliminate or mini-
mize adverse health or environmental
effects.
  (i) Provisions for long-term monitor-
ing and contingency  plans for correc-
tive  actions shall be  instituted where
necessary.
  (j) Planning  for. new facilities  and
services as described in subpart E of
this  part shall give priority to estab-
lishing replacement capacity for open
dumps.
  (k) Abandoned facilities that contin-
ue to produce adverse health or envi-
ronmental effects shall be subject to
classification according to the criteria
and  publication  in the  inventory  of
open dumps. The State plan shall pro-
vide for measures to insure that  ad-
verse health of  environmental effects
from  abandoned  facilities are mini-
mized  or eliminated.  Such  measures
may include actions by" disposal facili-
ty owners and operators, notification
of the general  public, adjacent resi-
dents  and other affected parties, and
notification of agencies responsible for
public  health and safety. Paragraphs
(d), (e), (g), (h),  and (j) of this section
do not apply to abandoned facilities.

§ 256.23 Recommendations  for closing or
   upgrading open dumps.
  (a) Each disposal   facility  in  the
State  should be considered to deter-
mine the potential for non-compliance
with the  criteria.  All facilities with a
reasonable probability for non-compli-
ance should be evaluated in detail and
classified according to the criteria.
  (b) All sources of information availa-
ble to  the State should be used to aid
in the  classification of facilities. Rec-
ords of previous inspections and moni-
toring, as well as new inspections and'
new  monitoring, should be considered.
  (c) For  each facility classified as an
open dump, a determination should be
made whether there  are  any alterna-
tives which could be utilized for all or
part  of the solid waste volume. Such
alternatives should include processing
and  disposal at  other facilities,  up-
grading the open dump, resource  re-
covery and resource conservation. This
determination  should  be  based  on
damages  from   allowing  continued
open dump operation, the cost of al-
ternatives, and the ability of the oper-
ator  of or the entity served by an open
dump  to utilize  the alternative. The
assessment  of alternatives should  be
coordinated with the facility needs as-
sessment described in § 256.41.
  (d) A determination should be made
of the feasibility of resource recovery
or resource  conservation to reduce the
solid waste  volume entering a facility
classified as an open dump; and, feasi-
ble measures to achieve that reduction
should be implemented.

§ 256.24  Requirements to prohibit the  es-
    tablishment of new open dumps.
  In meeting  the requirements of sec-
tion 4003(2) the State plan shall pro-
vide that:
  (a) The necessary State legislative or
administrative  authorities   are  ob-
tained to prohibit the establishment
of new open  dumps and require that
all  solid waste disposal be carried out
in compliance with the criteria.
  (b) The State regulatory powers nec-
essary to control the disposal of solid
waste (as described in § 256.20) are em-
ployed to insure that this requirement
is complied with.
  (c) The identification of responsibil-
ities, (as described in subpart B of this
part) and the planning for new facili-
ties and practices (as described in sub-
part E of this part) are carried out as
necessary to support this requirement.

    Subpart D—Resource Conservation and
       Raiource Recovery Program*

  NOTE.—This subpart-, addresses require-
ment (5) of section 4003 and the require-
ment in section  6002 for the procurement of
products  containing materials  recovered
from solid waste. This subpart also address-
es requirements (2) and (6) of section 4003
as they pertain to resource conservation and
recovery.

§ 256.30  Requirements.
  (a) In order to comply with sections
4003 (2) and (6), the State plan shall
provide for  a policy and strategy for
encouragement  of resource  recovery
and conservation activities.
  (b) In  order to comply with section
4003(5),  the State plan  shall  provide
that no  local  Government  within the
State  is  prohibited  under State  or
local law from entering into long-term
contracts for the supply  of solid waste
to resource recovery facilities.
  (c) In  order to comply with section
4003(6) and section 6002, the  State
plan shall provide that State procure-
ment practices require the purchase of
items  composed  of the  highest per-
centage of recovered materials practi-
cable,   consistent  with   satisfactory
levels of competition, availability, per-
formance standards and cost,  when-
ever Federal funds are used for such
purchase. This requirement is subject
to the  exclusions  and conditions  of
section  6002 of the Act, and  compli-
ance with this requirement may be de-
layed  until  after  the Administrator
issues guidelines  for procuring  agen-
cies under section 6002(e).

§256.31  Recommendations for developing
    and implementing resource conserva-
    tion and recovery programs.
  (a)  In order to encourage resource
recovery and conservation,  the  State
plan  should  provide for technical as-
sistance, training, information devel-
opment  and  dissemination,  financial
support programs, market studies and
market development programs.
  (b)  In order to  comply with the re-
quirement  of  § 256.30(b)  regarding
long-term  contract  prohibitions, the
State plan should provide for:
  (1)  Review  of  existing  State and
local  laws and regulations  pertinent to
contracting for resource recovery ser-
vices  or facilities.
  (2)  Reporting of all laws and regula-
tions  found to be in violation of this
requirement to the executive officer of
the governing body responsible for the
statute.
  (3)  Development of an  administra-
tive order or  a revised law or regula-
tion or any other preliminary step for
the removal  or amending  of a law  or
regulation in  violation of this require-
ment.
  (4)  Development of a  strategy- for
passage of legislation,  execution  of an
administrative order, or other action
that  would  prohibit  and/or remove
from  State or local law provisions  in
violation of this requirement.
  (c)  In meeting  the  requirement  of
§ 256.30(c) concerning  procurement  of
products containing recovered materi-
als the State  plan should  provide for:
  (1)  The development  of  a  policy
statement  encouraging  the  procure-
ment  of recovered materials, wherever
feasible:
  (2) The identification of the key pur-
chasing agencies  of the  State,  along
with potential uses of recovered mate-
rials by these  agencies;
  (3)  The development of a plan  of
action to promote the use of recovered
materials through executive order, leg-
islative initiative,  or other action that
the Sta'te deems necessary.
  (d)  In order to encourage  resource
recovery and  conservation, the.State
plan  should  provide for the elimina-
tion, to the extent possible, of restric-
tions  on the purchases-of goods or ser-
vices,   especially  negotiated  procure-
ments, for resource recovery facilities.
This should include:
  (1)  Review   of  existing State  and
local  laws pertinent  to  the  procure-
ment  of equipment and  services for
the design, construction and operation
of resource recovery facilities;
  (2) Listing of all laws that limit the
ability of Jocalities to negotiate for the
procurement of the design,  construc-
tion, or operation  of resource recovery
facilities.
                              FEDERAL REGISTER, VOL. 43, NO. 167—MONDAY, AUGUST 28, 1978

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                                                PROPOSED RULES
     !  < •.Yk-nment  of administrative
  . ;    jr  l-gisiation  or  other action
     tst,i;id  eliminate these  restric-

  •   T)-" •'lopment of a  strategy and
     f action for the execution of ad-
     •..r.itivc orders, the enactment of
   1.1' i-m, or other actions that would
    1 Hi  these restrictions.
     i'; •-> Plate plan should encourage
 -. ••'." ''lopiPciit of resource recovery
  '   r  ^ource  conservation  facilities
  . !->-:  i»roverab]e industrial wastes;
     ! ~i.ors;  ferrous  and nonferrous
       p,laas;  solid, liquid, or  gaseous
  ',-  -i'idges; and Lires. The following
  ••' !  N:  evaluated: Location  and
 1  '.'irtntion  requirements,  materi-
    •u! • nergy specifications  of  user
  :". '?-;•;;, minimum  quantity require-
       rrir-ing  mechanisms and long-
  ;•- "-(.tract availability.
 •, '  R.-source  recovery  feasibility
  'i.>s should be conducted in regions
  n-'' State in which uses or markets
 •  ;< <"0'. ered  materials or energy are
  jiu'ipd. These studies should review
 /ion? technological  approaches, en-
 • ,nfr<.°nta)  considerations,   institu-
 " --si  and financial  constraints, and
 onoivjif- feasibility.
 ' < • Source separation, recycling and
 • '.'!>'re conservation should  be uti-
"<-v 'Mi'  recovery of energy and materi-
!•-  i.-i ikl be utilized whenever techni-
•ii.  and economically feasible.-
 <"> Source separation, resource con-
-, (\anon and mixed  waste processing
•nicii;  should   be  combined   to
 •h.F.-i-f-  the  most effective resource
:<>. ;-t Cation and economic balance.

     • .;'i»tirl E—Facility Planning and
           implementation

 'IOTK -This  subpart  addresses  require-
.cm  (6) of section 4003 as it pertains to fa-
,- f, planning and implementation.

  •'• i;1  Requirements.
  a1  In order to comply with section
'•'..KG),  the  State plan shall  provide
 • adequate disposal facilities and for
   • :'i-e recovery  and conservation fa-
  ,'•; and practices necessary to Use
or dispose of solid waste in an environ-
mentally sound manner.
  (b) The State plan shall provide for
adequate  and appropriate  recovery,
storage, treatment and disposal capac-
ity for any  wastes  determined to  be
hazardous wastes.

§ 256.41  Recommendations for assessing
    the need for resource recovery and dis-
    posal facilities.
  (a) In meeting the  requirement for
adequate disposal and resource recov-
ery  facilities, the State plan should
provide for  an assessment of the ade-
quacy of existing facilities for recovery
and disposal and the  need for new or
expanded facilities.
  (b) The needs assessment  should be
based on current and projected waste
generation rates and on the  capacities
of presently operating and planned fa-
cilities.
  (c) Special handling needs  should be
determined  for all solid waste catego-
ries.
  (d) Impact on facility capacities due
to predictable changes in waste quan-
tities and characteristics should be es-
timated.
  (e) Environmental, economic,  and
other constraints on  continued oper-
ation of facilities should be assessed.
  (f) Diversion of wastes due  to closure
of open dumps should be anticipated.
  (g) Facilities and  practices planned
or provided for by  the  private sector
should be assessed.
  (h) The State plan should  provide
for the identification of areas which
require new capacity development.

§ 256.42  Recommendations for  assuring
    facility development.
  (a) The State plan should address fa-
cility planning and  acquisition for all
areas which are determined to Have in-
sufficient recovery and disposal capac-
ity in the assessment of facility needs.
  (b) Where facilities and practices are
found to be  inadequate,  the State plan
should provide for the necessary facili-
ties and practices to be developed by
responsible  State and substate  agen-
cies or by the private sector.
  (c) For all areas found to  have five
or fewer years of capacity remaining,
the  State plan should provide for (1)
the development of  estimates of waste
generation by type and characteristic,
(2) the evaluation and selection of re-
source recovery, conservation or dis-
posal methods, (3) selection of sites f6r
facilities  and,  (4)   development  of
schedules of implementation.
  (d).The State plan should encourage
private sector initiatives in order  to
meet the identified facility needs.
  (e) The State  plan should  provide
for the State  to  acquire facilities or
cause facilities to be  acquired in any
area having fewer than 2 years' of pro-
jected capacity.
  (f) The State plan should provide for
the initiation and development of en-
vironmentally sound facilities (includ-
ing  resource recovery facilities)  as
soon as practicable to replace all open
dumps  found to be without alterna-
tives.
  (g)  The  State plan  should provide
for the State, in cooperation  with sub-
state  or regional agencies, to establish
procedures  for  choosing which facili-
ties will get priority for technical or fi-
nancial assistance or other emphasis.
Highest priority should be given to fa-
cilities developed to replace or upgrade
open dumps.
  (h)  The  State plan  should provide
for substate or regional  cooperation
and policies for free and unrestricted
movement of solid waste across State
and local boundaries.

§256.43  Recommendations for  hazardous
   waste facility planning  and develop-
   ment.
  (a)  The  State plan  should provide
that facilities are available for the re-
covery, treatment,  storage  or disposal
of all  hazardous wastes generated or
disposed of in the State.
  (b) Upon determination of the exis-
tence of markets for hazardous waste
materials or energy usage, the State
plan should contain a strategy for en-
couraging such utilization of hazard-
ous wastes.

Subpart F—Coordination With Other Program*

§256.50  Requirements.
  Section 4003(1) requires the State
solid waste management plan to iden-
tify means for coordinating regional
planning and  implementation under
the' State plan. Section 1006 requires
the Administrator to integrate all pro-
visions  of this Act (including approval
of State plans) with other Acts  that
grant regulatory authority to the  Ad-
ministrator in order to prevent dupli-
cation of administrative and enforce-
ment efforts. In order to meet these
requirements:'«.
  (a)  The  State solid  waste manage-
ment plan  shall be developed in co-
ordination  with Federal,  State,   and
substate programs  for  air quality,
water  quality,  water  supply, waste
water treatment, pesticides, ocean pro-
tection, toxic substances control, noise
control, and radiation control.
  (b) The State plan shall provide for
coordination with programs under  sec-
tion  208 of the Clean Water Act, As
amended (33 U;S.C. 1288). In identify-
ing agencies for solid waste manage-
ment planning and implementation,
the State shall  review the solid waste
management activities being conduct-
ed by water quality planning  and man-
agement  agencies   designated  under
section 208 of  the  Clean Water Act.
Where  feasible, identification of such
                             FEDERAL REGISTER, VOL. 43, NO. J 67—MONDAY, AUGUST 28, 197«

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                                                PROPOSED RULES
                                                                    38545
agencies should be considered in the
identification process subpart B of this
part. Where solid waste'management
.and water quality agencies are sepa-
rate  entities,  necessary coordination
procedures shall be established.
  (c) The State plan shall  provide for
coordination with the National Pollut-
ant  Discharge  Elimination  System
(NPDES)  established   under section
402 of the Clean Water Act, as amend-
ed (33 U.S.C. 1342). The classification
of a facility for purposes of the  open
dump inventory and the issuance of
State compliance schedules for closing
or upgrading of a facility classified as
an  open dump shall be timed,' where
practicable, to coordinate closely with
the  issuance  of  a new  or revised
NPDES permit for such facility.
  (d) The State plan shall  provide for
coordination with activities for munic-
ipal sewage sludge disposal  and utiliza-
tion conducted under the authority of
section 405 of the Clean Water Act, as
amended (33 U.S.C. 1345), and  with
the  program for construction grants
for publicly owned, treatment works
under section 201 of the Clean Water
Act, as amended (33 U.S.C.  1281).
  (e) The State plan shall  provide for
coordination with  State .pretreatment
activities under section 307  of  the
Clean  Water  Act,  as amended  (33
U.S.C. 1317).
  (f) The State plan shall  provide for
coordination with agencies conducting
assessrhents of the impact of surface
impoundments    on    underground
sources of drinking water under the
authority of section 1442(a)(8XC) of
the  Safe  Drinking Water  Act  (42
U.S.C. 300j-1).
  (g) The State plan shall  provide for
coordination with  State underground
injection  control programs (40  CFR
Part  146) carried  out  under  the au-
thority  of the Safe Drinking Water
Act (42 U.S.C. 300f et seq.) and  with
the designation of sole source  aquifers
under section 1424 of that Act.
  (h) The State plan shall  provide for
coordination, where practicable,  with
programs under:
 '(1)  The Toxic Substances  Control
Act (15 U.S.C. 2601 et seq.).
  (2)  The Federal Insecticide, Fungi-
cide and Rodenticide   Act (7 U.S.C.
1362 et seq.).
  (3) The Clean Air Act, as amended
(42 U.S.C. 7401  et seq.) (incineration
and  open  burning  limitations under
State implementation plans).
  (4) The Marine Protection, Research
and Sanctuaries Act (33 U.S.C. 1420 et
seq.).
  (i) The State plan shall provide for
coordination, where  practicable,  with
programs of other Federal agencies,
including:
  (1)  Army  Corps    of   Engineers
(NPDES  permits,   wetlands,  flood
plains);
  (2) Department of the Interior
  (i) Fish  and Wildlife  Service (wet-
lands),
  (ii)  Office  of  Endangered Species
and Fish and Wildlife Service (solid
waste disposal in critical habitats),
  (hi) Bureau of  Mines and  Office of
Surface Mining (mining waste disposal
and use of sludge in reclamation),
  (iv)  U.S.  Geological Survey (wet-
lands, floodplains, ground water);
  "K3)   Department   of   Commerce,
NOAA   (coastal   zone  management
plans);
  (4) Water Resources Council  (flood
plains, surface and ground waters);
  (5) Department of Agriculture,  in-
cluding  Soil  Conservation  Service
(land spreading solid waste on food
chain croplands);
  (6) Federal  Aviation Administration
(locating landfills near airports);
  (7)  Department  of  Housing  and
Urban Development  (701 comprehen-
sive planning  program, flqod  plains
mapping);
  (8) Department of Defense (resource
recovery and solid waste disposal pro-
grams at various installations); and
  (9)  Department  of Energy (State
energy  conservation  plans under the
Energy Policy and Conservation  Act
(42 U.S.C. 6321)).

      Subpart G—Public Participation

§ 256.60  Requirements  for public partici-
    pation in State and substate plans.
  Ca) Public participation in the devel-
opment and implementation of State
and substate plans shall be  in accord
with 40 CFR Part 25i
  (b)  State  and  substate  planning
agencies shall:
  (1) Maintain a  current list of agen-
cies, organizations,  and individuals af-
fected by or interested in the plan,
  (2) Establish an  advisory  group, in
accord  with  40  CFR  25.3(d)(4),  to
make  recommendations   on  major
policy  and program decisions to offi-
cials responsible for plan development,
and
  (3) Provide  depositories of relevant
information in one or more locations
convenient to the interested  or affect-
ed public.
  (c)  State  and  substate  planning
agencies shall provide information and
consult with the public and the adviso-
ry group, established  under paragraph
(b)(2) of this section,  on plan develop-
ment and  implementation.  Provision
of information and consultation shall
occur both early in the planning proc-
ess (including the preparation and dis-
tribution of a summary of  the pro-
posed plan) and on major policy "deci-
sions made  during the course of plan
development,  revision and implemen-
tation. Planning agencies shall:
  (1) Publicize information  in news
media  having broad audiences in the
geographic area,
  (2) Place information in depositories
maintained under paragraph (b)(3) of
this section,
  (3)  Send  information  directly  to
agencies, organizations and individuals
on  the list  maintained under para-
graph (b)(l) of this section, and
  (4) Prepare and-make  available to
the public a summary of public partici-
pation in the planjn accord with 40
CFR 25.15.
  (d)  State  and substate  planning
agencies shall conduct public hearings
(and  public  meetings,  where  the
agency  determines there  is sufficient
interest) in accord with 40 CFR 25.3(d)
(2)  and  (3) and all applicable State ad-
ministrative  procedures.  The purpose
of the hearings and meetings is to so-
licit reactions and  recommendations
from interested or affected parties and
to explain major issues within the pro-
posed plan. Following the public hear-
ings, a summary of agency response to
public  views  shall  be  prepared and
made available to the public in accord
with 40  CFR  25.15.

§ 256.61  Requirements for public partici-
    pation  in-  (he  annual State work pro-
    gram.
  (a) Public participation in the devel-
opment of the annual State work pro-
gram shall be in accord with 40 CFR
Part 25.
  (b) A  public participation work plan
developed  in accord  with  40 CFR
25.11(b)  shall be  included  in  the
annual State work program.
  (c) The  State shall consult with the
public,  including the  advisory  group
established under § 256.60(b)(2), in the
development  of the  annual work pro-
gram. One month, prior to submission
of the draft  work program to the Re-
gional  Administrator,  as  required  by
40  CFR Part 35, the draft work pro-
gram  shall be made available to  the
public at the  State information depdsi-
tories maintained under §256.60(b)(3).
The public shall  be notified  of  the
availability of the draft work program,
and a public meeting shall  be held if
the planning agency determines there
is sufficient interest.
  (d) The State shall comply with the
requirements of Office of Manage-
ment and Budget Circular No. A-95.
  (e) Copies of the final work program
shall be placed in the State informa-
tion depositories  maintained'  under
§256.60(b)(3).

§ 256.62  Requirements for  public partici-
    pation in State regulatory development.
  (a) Public participation in the devel-
opment of State regulatory  powers
shall be in accord with 40  CFR Part
25.
  (b) The  State shall conduct public
hearings (and public meetings where
the State  determines there is suffi-
cient interest) on all proposed State
                             FEDERAL REGISTER, VOL. 43, NO.  167—MONDAY, AUGUST 28, 1978

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38546
PROPOSED RULES
                    legislation and regulations, in accord
                    with 40 CFR 25.3(d) (2) and (3) and all
                    applicable State administrative proce-
                    dures, to solicit reactions and recom-
                    mendations.  Following   the  public
                    hearings,  a summary of  agency re-
                    sponse to public views shall be pre-
                    pared and made available to the public
                    in accord with 40 CFR 25.15.
                     (c) In advance of the hearings and.
                    meetings required by paragraph (b) of
                    this section, the State shall prepare a
                    fact sheet on proposed regulations or
                    legislation, mail the fact sheet to agen-
                    cies, organizations and individuals on
                    the     list     maintained    under
                    § 256.60(b)(l), and place the fact sheet
          in the State information depositories
          maintained under § 256.60(b)(3).

          § 256.63  Requirements for public partici-
             pation in the permitting of facilities.
            (a) Before a permit application for a
          resource recovery or disposal facility is
          approved by the State, a public hear-
          ing shall be conducted to solicit public
          reaction and recommendations on the
          proposed permit application.
            (b)  This  hearing shall be  held in
          accord with 40 CFR 25.3(d)(2) and all
          applicable State and local administra-
          tive procedures.

           [PR Doc. 78-24166 Piled 8-25-78; 8:45 am]
                               FEDERAL REGISTER, VOL. 43, NO. 167—MONDAY, AUGUST 28, 1978

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                                                                  437
                State Solid Waste Management Plans
             Discussion Leader:  Mr. George A. Garland
Question:  As abandoned facilities,  not only landfill sites but also other

           solid waste management facilities should be considered.   For

           example, refuse collection carriers,  incinerators,  leachate

           treatment facilities and composting plants may be important

           to be considered.  These should not  create new solid waste

           problems.


Answer:    We recognize that there are a number of other types of solid

           waste management facilities.  By and large, the environmental

           effects from these facilities are handled under other environ-

           mental acts such as the Clean Air Act for incinerators  and

           the Clean Water Act for effluent from leachate treatment facili-

           ties.  For refuse collection we do have a focus on  productivity

           and safety because we recognize that there is bulk  in the

           system.  However, under the Resource Conservation and Recovery

           Act, we do focus primarily on the environemntal effects from

           land disposal.

Question:  We may introduce a Government Plan to prepare final disposal

           sites (Phoenix Plan to obtain large scale landfill  sites).

           In the future, regional,  national or international  cooperation

           for solid waste management in siting and facility development

           is more essential.

Answer:    In this country, we have had a policy of relying on the private

           sector and not encouraging federal interference in  final disposal

-------
                                                                     438
           sites.   However,  we are recognizing that  because  of  severe



           difficulties,  especially with hazardous waste facilities,



           we have to give more consideration  in  this direction.   We



           definitely are in agreement that in the future,  regional,




           national and international  cooperation in siting  and facility



           development is essential.  The public  is  insisting-on  better




           technology and information  about what  we  are doing.  Sites



           are becoming fewer and fewer so we  are going to  have to cooper-



           ate more.  Many resource recovery facilities are  now being



           built in this country and we are anxious  to learn from the



           experience with these facilities.  But because the federal



           government is not in a position of  paying for these  facilities



           we have to wait for this experience before requiring that




           others follow suit.  I would like to defer to Mr. Peter who



           is Director of the Resource Recovery Division for any further



           remarks on our overall policy on resource recovery.





Comment by Mr. Peter:  I'll  touch on many of these issues when  I  present



           my paper later this morning, but one of the difficulties of



           getting more of these plants on line is economics.  The posture



           of this government is that, unlike  the sewage treatment facilities



           where there is assistance from the  federal government  for



           construction, we  believe that industry has a major role in



           working with communities in arriving at solutions.  There  is



           an economic incentive in that direction.   We do  provide a



           considerable amount of planning assistance and information

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                                                               439
dissemination to the states and local governments.   But we



recognize that one of the major problems we have is the



difficulty of the planning process.  And that is the major




effort of the federal government at the moment—providing



that kind of planning assistance to the states.   We do not



have authority under RCRA to provide financial assistance



for either the acquisition of sites or for construction



of these facilities.

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                                          440
  MARKETS FOR RECOVERED MATERIALS

        A Current Overview
       ALBERT A.  PETER, JR.

         Prepared for  the
 Fourth Japanese-American Conference
      on  Solid Waste  Management
         Washington, D.C.,
            March 1979
U.S. ENVIRONMENTAL PROTECTION AGENCY.

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                                                   441
             MARKETS FOR RECOVERED MATERIALS

                   A Current Overview

                 by Albert A. Peter,  Jr.



     For the past half-century,  this  country has experienced

unprecedented industrial growth,  punctuated by sometimes

unbelievable technological achievements.   From this period,

and from the pioneer spirit which preceded, an American

ethic evolved which demanded that we  be the first and the

best.



     More than a decade has passed since the ecological .

movement in America cried out for a change in the primitive

practices by which the Nation was handling its mounting

solid waste problems.  Aside from the problems, however, the

oil crisis of the early 1970's created an awareness of vast

resources which were going to waste in the countless "mountains"

of garbage around the country.  In spite of these motivations

and the "American ethic," nothing much has happened in the

way of tangible change.  And for many it is bewildering to

realize that at this rather late date, the Nation which put

men on the moon has less than ten operating resource recovery
     Mr. Peter is Director,  Resource Recovery Division,  Office
of Solid Waste, U.S. Environmental Protection Agency,  Washington,
D.C.

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                                                     442





                            2




plants, while European and Far Eastern countries boast more



than 200 such plants.  Although this observation has been



made many times, it should be understood that the complexi-




ties of differing institutional and political systems, and




underlying economic conditions rather than technology, are




the principal factors which steer nations in different




directions as they search for solutions and the paths for




some are simpler than for others.








     The fact remains, however, that progress in resource



recovery has been disturbingly slow in this country; that




.Americans seem to perceive little economic advantage to



conserving their natural resources by reusing their waste



materials.  Of the 148 million tons of municipal solid waste



generated in 1977 in this country, only 11 million tons, or



7.5 percent, were reclaimed for use by industry.








     At a recent conference cosponsored by the U.S.



L,ii\•'T ronmental Protection Agency and the Brookings Institution




   Washington, D.C., scholars from the academic fields met




v-* !i high-ranking representatives from government and industry,



   ;.;:g with public-interest groups with a deep sensitivity to




environmental concerns.  The conference dealt with very




fundamental issues and questions, some of which included:








     o    Is there a real need to conserve?




     o    Are the sources of raw materials being depleted?

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                                                     443




                            3



     o    What are the worldwide implications of an aggressive




            conservation program?




     o    What is the role of'the Federal government?



     o    Is sufficient information available to the




            policymakers?








It is interesting to note that such broadly based questions




are being discussed some ten years after the national




awakening mentioned above.








     While many of these questions will be debated for  quite



some time, come, the conferees did identify certain areas of



general agreement:








     o    That with the exception of three particular materials,



          namely cobalt, platinum, and chromium,  and setting



          aside the issues of economics and world politics,



          there is an abundant supply of known reserves of



          virtually all nonfuel minerals and timber to  meet



          worldwide requirements well into the next century;








     o    That there is no "scarcity crisis" around which a



          nation must build a dynamic conservation program;








     o    That there is no system of "absolutes"  which  would



          either justify a total disregard for the need to

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                                                        444




                            4




          conserve, or a use of every measure of conserva-




          tion, regardless of cost.








     Despite favorable economics and abundant supplies of




raw materials, a good case for conservation was advanced




with the recognition that land itself is a resource to be




considered in the disposal process.   Today, close to 95




percent of the Nation's annual municipal refuse burden of




148 million tons is going directly to the land for disposal.




While evidently not a universal problem, landfill siting is




a geographically sensitive issue because the availability of




land is dwindling at a rapid rate in many parts of the




country.  A case for conservation and recycling was also




supported by recbgnizing that our heavy dependency on energy




imports (some 80 percent of our domestic petroleum needs)




could be reduced considerably by better management and by




capturing the vast energy potential in the Nation's municipal




waste stream.








     The environmental movement of the mid-1960's focused




much of its attention on what was perceived as a moral




issue relating to the American lifestyle of waste, the




almost wanton consumption of natural resources, and the




fast-growing generation of staggering volumes of solid




waste.

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                             5



     There evolved from  that period  a  government respor -•



the form of several pieces of  environmental  legislation,  :



first of which, passed in 1970, was  the  Resource Recovj -




Act (RRA) .  That Act gave the  Environmental  Protection



Agency a broad mandate to study the  problem  of  solid war-.



and to undertake a number of pilot^ projects  to  demonstrate




technologies which might possibly contribute to the sol ••



Contrary to most environmental legislation of that, PCM, !."•>:,



the RRA did not contain  any  regulatory provisions de;> i . ;u,




directly with municipal waste.  The  years between Lhe pa-.::,



of RRA and the passage of the  Resource Conservation a:,:i



covery Act of 1976 were  devoted primarily to basic rese.-j; ..



as well as full scale demonstrations,  both technical aii;.:




economic, by which materials and energy  could be recox .v, I




from the municipal aste  stream.








     That chapter in our history is  closed and  this Kt,:_'-.•



is now facing a second generation of activities in i c;:. ^.;; - •



recovery.  We now have some  25 major new mixed  waste i i. , !



ties well along in the planning stages,  and  10  others .,.-



into the construction phase.   It is  further  estimate] th ,i



by 1985 about 40 to 50 energy-related  resource  recovery



plants will be in operation.   Municipal  separate coll o<,r i _,




programs which recover materials for recycling  have 11; •. :




from 2 in 1972 to 220 in 1978.

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                                                        446





                            6




     Even with this apparent upsurge in activities,  one of




the most serious and perplexing problems hampering our




efforts to reduce the volume of waste by source separation




programs, or by recovering materials through processing




plants, is the absence of viable markets for some of the




materials thus produced.  Looking back over the last decade,




the technologies and techniques employed to retrieve materials




from the waste stream were widely tested, and much progress




was made refining those methods which appeared to produce




marketable products.  But, in a business sense, while signi-




ficant progress has been made on the supply side of the




resource recovery equation, virtually nothing has appeared




to change the demand side.








        STATUS OF MARKETS FOR RECOVERED MATERIALS
Paper
     Paper is the largest single segment of the waste stream,



constituting between 30 and 45 percent of the average commu-



nity's waste collections.  Paper is also the most commonly




recycled material.  Of the 11 million tons of materials



reclaimed annually, 93 percent is paper.  The national




recovery rate for post-consumer paper, 16 percent (excluding




export), has remained virtually unchanged over the last ten

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                                                              447
                            7

years.  Although that in itself may appear to be discouraging,

it must be pointed out that the years before 1968 witnessed

a steady and sometimes precipitous decline.  The arresting

of that decline was a significant step forward.


     The recyclability of wastepaper is determined first by

its grade.  Paper is recovered at the point of generation,

usually the home, in the case of newspapers; the office, in

the case of high-grade pulp substitutes,  and commercial

facilities such as grocery and department stores, in the

case of corrugated paper.  Present recovery rates for the

major paper grades and the products in which they are used

vary from 8 to 21 percent (Figure 1).

                        FIGURE 1

       WASTE-PAPER RECYCLING RATES AND END PRODUCTS (1977)

Waste-Paper Grade        Recycling Rate      Final Destination

Newspaper                     21%            Boxboard

                                             Newsprint

                                             Cellulose Insulation

Office paper                  13%            Tissue

                                             Boxboard

                                             Printing/Writing

Corrugated                    26%            Corrugated Medium

                                             Boxboard

Other                          8%            Boxboard

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                                                         448





                            8




     Obviously, an established market for wastepaper exists



and has existed for years.   Some 16.3 million tons  of indus-




trial capacity are dedicated to the production of products




from wastepaper.  Unfortunately, the existence of an estab-



lished market with established buyers, standard specifications,



and committed manufacturing capacity does not assure a




stable market for post-consumer waste.








     The used corrugated,  newsprint, and, to a lesser extent,




the high-grade ledger and  pulp substitute grades are all



extremely sensitive to fluctuations in the Nation's economy.




To quote a 1976 EPA publication:








     Prices of wastepaper  have historically been



     unstable.  Figure 2 illustrates the wastepaper price




     index over the period 1950 to 1975.  The two major



     anomalies correspond  to very dramatic periods  in recent



     economic history—the Korean War and the short-lived



     1973-74 economic boom.  On such occasions, demand



     momentarily spurts ahead of installed capacity.




     Capacity utilization  rates approach 100 percent and




     industries become willing to use secondary materials



     as the input of last  resort.  This, in turn, creates




     a sharp increase in the price of secondary material.



     The correction—increased supplies of wastepaper,

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                                                         449




                            9



     increased virgin material availability,  or downturn




     in the economy—results in an equally rapid drop in



     prices.








     The primary cause for this sensitivity to overall




economic pressures relates to the two major markets for




wastepaper, namely, boxboard and construction materials.  In



an expansionary economy, housing starts (construction material)




generally rise and more products are sold (requiring more




boxes); conversely, in a recessionary economy, consumer



products and construction materials are usually the first



areas to feel the economic slowdown.








     The general state of the economy is not the only factor



influencing wastepaper prices.  Part of the reason for the




dramatic upturn of prices and tonnage of recycled paper in



1973-74 was the Canadian paper unions strike which lasted



for many months.  The dramatic downturn of prices in Sep-



tember 1978 was caused because the cellulosic insulation



industry vastly overestimated the potential demand for home



insulation, in spite of the growing national concern for




energy.








     The capacity decisions of foreign governments and



industries have a large effect on domestic paper prices,



and wastepaper export tonnages have varied widely (Figure 3).

-------
450

-------
                                                          451




                            11




                        FIGURE 3




     Year                               Tonnage




     1972                               415,000




     1973                               683,500




     1974                             1,300,000




     1975                               861,000




     1976                             1,273,000




     1977                             1,500,000








Tonnages are expected to rise significantly after 1980 when




announced new capacity will be in place in the Far East.




The effect could also be negative, of course,  if there is a




repeat of the situation in 1977 when the Swiss government




decided to dump thousands of tons of market pulp on the




world market.  With that decision, white ledger prices went




from an average of $120 per ton to $95 per ton in two months.








     The volatility of the paper market is probably the




major inhibitor to expanded paper recycling in the United




States.  Manufacturers are most reluctant to commit to new




capacity when raw material input cost may be a money-making




$20 per ton in June and a money-losing $45 per ton in




September.

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                                                         452




                            12




     In 1970, there were two major arguments against




recycling put forth by virgin fiber-paper manufacturers:




The first argument suggested that all the paper that is




recoverable is being recovered,  and that the paper which




remains in the waste stream is too contaminated to be used




in manufacturing processes.   This argument was largely




disproved in 1974 when recovered wastepaper tonnages




doubled and, in some cases,  tripled from month to month.




It is clear, therefore, that when the price is right, the




paper will come out of the waste stream and be used.








     The second argument contended that the paper market  is




too volatile, and the level of risk too high to justify




investment.  Today, for most paper grades, there is clear




evidence to support this argument.
Glass
     Glass constitutes approximately 9 percent by weight of



the municipal waste stream.  About 90 percent of this fraction




is container glass, approximately half of which is beverage




containers.








     Since 1960, the amount and relative percentage of glass



in the waste stream has risen rapidly due to the introduction

-------
                                                          453




                            13



of the one-way beverage container.  One of the major motiva-




tions of the returnable beverage container movement in this



country has been to reduce this fraction of waste.








     Efforts to recover post-consumer glass containers began




in 1970 as a part of the overall environmental movement-



Consumers were asked to bring glass containers and sometimes



cans along with their paper to "reclamation centers."  At



the present time, it is estimated that these centers recover



approximately 1 to 2 percent of all waste glass.   Curbside



collection of glass, again along with other material, is




being practiced in 23 communities in California and the



northeast.








     Mechanical recovery of glass in mixed-waste processing




facilities has been tried in pilot plant operations using the



froth flotation method.  The color-mixed cullet product



("cullet" is the glass industry's term for crushed glass)



produced by this system does not consistently meet the very



stringent specifications required by the industry.   Because



of this issue and the costs of recovery, mechanical recovery



of glass for use in the container industry is not feasible



at this time.  Furthermore, markets for mixed-color glass




are very limited.  Lower grade uses of this material in such




products as brick., concrete block, or paving materials appear



to be technically feasible, but there has been little or  no

-------
                                                          454




                            14




interest on the part of manufacturers due to the ready availa-



bility of the inexpensive virgin materials traditionally



used in those products.








     At present, the only viable waste-glass market is with



the glass container manufacturers.   While the industry as a



whole expresses interest in cullet  as a source of raw material,




in only two sections of the country is there truly a demand



for waste glass.








     In California, glass is recovered for use in the




manufacture of wine bottles.  Mixed-color cullet is suitable



for these bottles because they are  either green (the color




best able to absorb cullet variations)  or so-called "eco-




color," a clear but slightly greenish color.  Although there



is a strong market, it is saturated by the present supply,



and opportunity for expanded glass  recycling in California



seems limited.








     Glass is also in demand in the northeastern States,




largely because of the air pollution problems of the largest




glass manufacturer in the area.  The use of cullet in large



quantities (40 to 60 percent of the mix)  significantly




reduces stack emissions from glass  furnaces.  Faced with an

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                                                         455





                            15




enforcement order from the State of Connecticut environmental




protection agency, the manufacturer agreed to the purchase




and use of 6,500 tons per month of cullet to lower its emissions,




As a result, the price for waste glass in the northeastern




States has risen from $20 in 1975, to $35 or $40 per ton




today.  Much of the cullet received is glass returned through




bottle deposits in Vermont and Maine.  Again, the saturation




point has been reached, and little expansion is expected.  A




major New York and New Jersey manufacturer is now seriously




considering following the previous example to solve its air




pollution problems.








Aluminum








     According to aluminum association figures, 25 percent




of all aluminum containers are recovered from the waste




stream.  In 1977, some 140,000 tons of aluminum were re-




covered (mainly cans), and the amount of waste aluminum




flowing back to the aluminum industry is startling con-




sidering that almost none was recovered ten years ago.








     At the present time, aluminum is recovered only through




source separation.   Individuals and groups are paid $.17 per




pound (up from $.10 in 1970)  for post-consumer aluminum




scrap at industry redemption centers all across the country.

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                                                        456



                            16



The high value of aluminum cans stems from several facts.



First, the various types of ferrous cans,  the aluminum can




is a high quality alloy aluminum and directly replaces



virgin aluminum for cans with almost no processing.   Economics



strongly favor aluminum can recycling with virgin aluminum




alloy for cans valued at well over $1,000  per ton.  The




second, and perhaps a more important reason for the  growing




value of aluminum scrap is that recycling  aluminum consumes




95 percent less energy than producing it from virgin bauxite.








     Efforts have been made to develop mechanical aluminum



recovery systems for use in mixed-waste processing plants.




The most hopeful of these, the eddy-current separator, appears



to recover an acceptable grade of aluminum or mixed  non-



ferrous metals.  Unfortunately, only 30 to 50 percent of the



available aluminum is recovered, and the cost of operating



the system appears to outweigh the revenue received  for the



very small amount recovered.








     While aluminum must be considered the biggest recovery




success story of the past decade, it must  be noted that this




material constitutes only about 1 percent  of the municipal




waste stream, making its relatively high recovery rate




comparatively unimportant to the local public works  director.

-------
                                                        457
                            17

Ferrous Materials


     Ferrous materials recovered from municipal waste consist

almost entirely of "bi-metal" beverage container cans or

"tin" food cans.  The so-called bi-metal can actually con-

sists of four metals: steel, tin,  lead, and aluminum, and

the "tin" can is actually a steel  can with a thin tin coating,


     In the early 1970's, the recovery of steel products was

considered to have great potential,  largely because of the

magnetic property of the material.   Experiments with various
industrial magnets were conducted  at landfill sites and in

mixed-waste processing plants.  By 1976, 36 ferrous recovery

facilities were in operation.  The quality of the material

recovered varied widely from facility to facility, but the
more sophisticated units produced  a comparatively clean
grade of scrap.


     The markets for this post-consumer can scrap were the
copper precipitation mines in the  southwest and steel mills
and detinning plants around the country.  Unfortunately,

problems have developed in all three markets.


     o    Copper Precipitation; Ferrous cans,  even highly

          contaminated ferrous cans, meet all quality

          specifications for the copper precipitation

-------
                                           458
                   18




 specifications for the  copper precipitation



 industry.   Unfortunately,  the demand  for  copper



 has been declining since  1974.  The need  for



 precipitation iron has, of course, declined



 with it.  The largest recoverer of ferrous cans in




 the United States, Los  Angeles Bi-Products, with



 four plants in California  has gone out of business




 and the market for ferrous cans has almost com-




 pletely dried up in the west.  In addition, the




 copper precipitation industry is gradually shifting



 to the liquid ion exchange technology, which  does



 not use cans at all.








 Detinning  Industry;  Detinners are found  in cities




 where there are major can manufacturers and steel



.mills.  The steel mills produce tin plate which



 goes to the can manufacturer.  The can manufacturer



 produces cans and large amounts of tin-plate  scrap,



 which it sells to the detinner.  The  detinner




 removes the tin from the  steel and sells  both to



 the steel  mill.  At first, this appeared  to be the




 perfect market for post-consumer ferrous  cans.



 Unlike the industrial scrap product from  the  can




 manufacturer, however,  the municipal  scrap con-

-------
                                                        459
                            19
          tained in the bi-metal can.  Both the lead and the
          aluminum contained in the bi-metal can are con-
          taminants to the detinning process.  A number of
          detinners have experimented with this scrap but
          almost none are now interested in purchasing the
          material.

     °    Steel Mills:  Both aluminum and tin are contaminants
          in steel making.  Thus the bi-metal can is also
          unwanted in this market.  At the present time, a
          few steel mills accept scrap cans from small
          recycling centers and four mixed-waste processing
          plants.  Confronted with large amounts of this
          material, the mills would have to refuse to accept
          it since only miniscule amounts are needed.

     Of the 36 magnetic separators operating in 1976, only
10 remain, and the vast majority of source separation programs
have stopped attempting to recover these scrap materials.

     It would appear that little will occur to enhance the
prospects for the recovery of ferrous cans unless the bi-
metal can is removed from the marketplace, or until the
steel industry undergoes technical changes enabling it to
accommodate larger quantities at higher prices to suppliers.

-------
                                                      460
                            20
                         SUMMARY


     Today, the markets for recovered municipal scrap are at
various stages of development, and the future is very uncertain,
EPA believes the following synopsis to be reasonable.


     o    Paper;  Most major grades of scrap paper will
          continue to be volatile in price.   The early
          1980's will see increased demand for newsprint,
          due to the opening of a new 325 ton-per-day
          secondary newsprint mill in Georgia and new
          capacity in the Far East.  There will probably be
          much pressure from domestic manufacturers to
          impose export quotas should decreased supplies
          cause prices to rise rapidly.


     o    Aluminum;  Prices received for scrap aluminum
          will probably continue to rise, as will the
          recovery rate.  National beverage container
          legislation, should it pass, will dramatically
          increase the amount of aluminum recovered from
          the waste stream.


     o    Glass;  There has been much hope over the last
          decade that the glass-container industry would

-------
                                                         461
                            21
          find true economic value in the use of cullet
          from the municipal waste stream.  To date,  this
          happened in only two instances.  There is little
          indication of rapid progress in this area.


          Ferrous;  As long as the bi-metal can remains a
          part of the ferrous fraction of solid waste,
          there will be little or no potential for expanded
          recovery of this material under present user-
          industry technologies.
                       CONCLUSIONS


     In the last decade, we have learned that most major
materials in the waste stream can be recovered and processed
to meet industry specification.   Unfortunately,  we have also
learned that, in almost every case,  the use of virgin materials
is more economical for industry.  Industry will retain the
principal role of developing the technology for materials
separation from mixed waste.  The Federal government will
continue a modest program of basic research,  principally
related to the environmental aspects of that effort.   The
Federal government will also continue its major programs to
assist State and local governments in their difficult and
complex plans for resource recovery programs.

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                                                        462



                            22




     There is a possibility that U.S.  Federal government



policies could considerably alter the  economic prospects for



some recyclable materials over the next decade.   For example,




a nationwide system of beverage container deposits could




have the almost automatic effect of source separating 90 per-



cent of the aluminum cans, steel beverage containers, and




nonrefillable glass and plastic beverage bottles from the



Nation's waste stream.








     There is no guarantee that all these materials would,




in fact, be purchased under today's markets,  particularly by



the steel and glass industries.  However, it  is not unlikely



that steel and glass manufacturers would seriously rethink



their raw materials procurement policies, as  a competitive



strategy in maintaining container market shares versus the



highly recyclable aluminum can.  The latter would receive an



undeniable boost by a deposit law.  In the absence of national



legislation, a further proliferation of State-level deposit



laws would have substantially the same effect.








     In addition, there are a host of other policy changes,



either recently enacted or currently under consideration by



the Federal government.  These include:








     o    reducing the favorable tax-subsidy  position of




          virgin domestic raw materials;

-------
                                                          463




                            23




     o    improving the railroad freight-rate position of



          recycled materials by prohibiting discriminatorily




          high rates for them;








     o    sharply curbing environmentally unsound landfill




          practices through Federal guidelines;








     o    providing investment tax credits for equipment



          used in recycling operations;








     o    encouraging local user fees for solid waste



          management services;








     o    providing continued Federal research and development




          programs to encourage technology changes;








     o    expanding Federal technical assistance to State and



          local governments as well as the private sector to



          stimulate the transfer of information;








     o    instituting Federal procurement policies designed



          to demonstrate the feasibility of using products




          with higher secondary material content.








     While none of these changes alone is going to have a



very large impact on United States material use policy or

-------
                                                         464

                            24

material recovery statistics, several of them taken together

may well provide the needed stimulus to turn the flat curve
                      I
of material recovery upward during the coming decade.

-------
                                                                              465
                    Markets for Recovered Materials, A Current Overview
                       Discussion Leader:  Mr. Albert A. Peter, Jr.
Comment:   From the questions that have been prepared in response to my
           paper, I gather that there is a concern in Japan for bulk
           material (refrigerators, etc.)
Comment:   Sulky waste is a difficult problem in Japan.   Under our laws
           municipalities are supposed to pick up the bulky waste.  But
           because of the high volume, they have some difficulty.  The
           private sector is also supposed to be handling bulky
           waste  but they have the same problems.
Question:  In Japan,  the disposal of domestic bulky refuse (for example,
           TV's, washers, etc.) is the responsibility of municipalities
           in general.   However,  it is becoming a burden to them year
           after year from the viewpoint of disposal cost.  We would
           like to know about the following matters in the U.S.:  How
           is the flow of domestic bulky refuse?  If municipalities
           have a charge system,,  do they collect any charge to dispose
           of domestic  bulky refuse?  If they collect some charge, is
           there any difference in charge by the weight of refuse or
           by the type of refuse?  Is there any other way to recover
           such bulky refuse by manufacturers or recycling agents?  If
           there is,  how is the charge system?
Answer:    Most of the municipalities in this country do not collect those
           bulky items as a matter of routine.  If you place these items
           out by the trash cans, they will not pick them up.  For the

-------
                                                             466
most part, the homeowner must call a private hauler for



collection of the bulky items; or in some cases, the




municipalities will pick them up for a special fee.  Or,



the bulky item can be taken to the nearby disposal facility.



There they are either placed in the landfill or set aside




and later sold to perhaps a scrap dealer.  Many of these



old items are disposed of by the purchase of the new item—



where the supplier of the new refrigerator, for example,



will pick up the old one when he delivers the new refrigerator.



The supplier will then hold it in his store until he has



accumulated enough to sell the items to the scrap dealer.



The private hauler will charge a fee generally based on the



weight of the object—ranging  anywhere from two to fifteen



dollars.  Occasionally a city will have to accommodate



community practice.  We still have some minor midnight dump-



ing going on; you will find stoves and refrigerators dumped



along the roadside or in empty lots.  So, some communities



have periodic clean up campaigns at which time they will



send trucks to pick up these items.  There is one other



activity in this country which is quite common but I don't



have any statistics as to what impact it has on the waste



stream.  This activity is conducted by volunteer groups.



They rework used machines, repair them and resell them.



Although I don't know statistically how large this operation



is, they are quite prominent in major cities across this



country.

-------
                                                                  467
Question:  Do other sections of the U.S.  Federal Government (for example,



           the Department of Commerce) have any program to expand



           recycling markets for recovery materials?  In Japan,  there



           is hardly any effort.



Answer:    They are supposed to.  Under the RCRA law, the Commerce



           Department is instructed to encourage the commercialization



           of proven—and the work proven is significant—resource



           recovery technology by doing four things: (1)  develop and



           supply  accurate specifications for recovered materials;  (2)



           stimulate the development of markets for recovered materials;



           (3)  promote proven technologies; and (4) provide a forum



           for the exchange of technical and economic data that relates



           to resource recovery facilities.  The Bureau of Standards,



           which is part of the Department of Commerce, has been work-



           ing on the specifications but progress has been slow because



           this is a highly complex subject.  The Department of Commerce,



           like most other agencies, has the problem of inadequate



           resources to accomplish everything for which they are respons-



           ible.  So, thus far, we have not seen much come out of these



           four programs.  There is, however, within the Department  of



           Energy, two mandates that were included in the recent energy



           legislation.  One has to do with an additional 10% tax invest-




           ment credit for equipment that is purchased for resource



           recovery; this means that they deduct considerably more from




           their income tax on that equipment.  And the second requires

-------
                                                         468
the Department of Energy to set what they call "voluntary



targets" for various industries for the use of recovered




materials.  But we don't hold out too much expectation at



this point as to whether this latter effort will have a




significant impact on resource recovery.

-------
                                                         469
                      RECOVERING ENERGY
                 FROM MUNICIPAL SOLID WASTE

          A Review of Activity in the United States
     Interest in recovering energy from municipal solid
waste has increased tremendously over .the past several
years.  Processes which were originally developed to ease
the environmental burden of waste disposal have suddenly
become sought after as a source of relief for increasingly
scarce energy shortages.  The escalating demand for systems
to convert waste to energy has stimulated such a rapid pace
in developing new technology that it has become very difficult,
if not impossible, to keep informed.  Techniques which were
unpopular in 1970 are being vigorously pursued in 1977.  And
other techniques which were only concepts on paper in 1970
are already being built on large scale in facilities perceived
as second- and third-generation designs.  "New and improved"
designs are being built even before tests are completed on
earlier designs.
         A Paper by David B» Sussman and Steven J. Levy
            Environmental Protection Specialists
                 Resource Recovery Division
                   Office of Solid Waste
        United States Environmental Protection Agency
                      Washington,  D.C.

-------
                                                     470
     From all this frenzied activity/  several concepts have



emerged that seem to be the most promising.   This paper will



review those various alternatives and attempt to place them



in perspective with regard to their status in the United



States.  The four alternatives for energy recovery of utmost



current interest are:







     1.   mass burning of unprocessed waste in heat recovery



          furnaces  (waterwall combustion units);







     2.   mass burning of unprocessed waste in small, modular



          starved-air, two-chamber incinerators;







     3.   the mechanical conversion of the organic portion



          of municipal solid waste into a refuse-derived



          fuel  (RDF) that is combusted as a primary fuel in



          a dedicated boiler or as a supplemental fuel along



          with coal in an existing boiler; and







     4.   the conversion of solid waste to other fuel forms



          through pyrolysis.

-------
                                  471










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-------
                                                         472




     Before examining the individual systems it is important



to first understand the nature of the material they will be •



handling.  Unfortunately, very little waste characterization



information is available for the specific citites included in



this paper.  In lieu of this, the following is based upon



the average American waste stream.








               Waste Quantity and Composition








     The U.S. Environmental Protection Agency has estimated



that about 115.4 million tonnes  (128.2 million tons) of



municipal wastes were generated from residential and commercial



sources in the United States in 1975 (1.45 kilograms or 3.2



pounds per person per day).  The quantities of particular



wastes found in these waste streams were determined (see



Table).  Quantities were also determined for the total



weight of the material "as generated," i.e., the weight of



the material before it was mixed with other wastes and "as-



disposed," the weight of the material after it was mixed in



trash cans and collection trucks.  The difference between



the two is the result of the migration of moisture from the



wetter materials  (food and yard wastes) to materials that



absorb moisture  (such as paper) and to products to whose



surface the moisture adheres  (such as glass and metals).



Excluded from the study were industrial and agricultural



wastes, sewage sludge, animal wastes, abandoned automobiles,



ashes, street sweepings, and construction and demolition



debris.

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                                                            473
                         Background
     The primary motivation for burning solid waste in the

United States has been, until recently, volume reduction, to

ease the burden of solid waste disposal.  In contrast to

most European countries, where both power generation and

waste disposal are managed by local governments, the waste

disposal function in the United States has been managed

almost exclusively by local governments and has been dis-

tinctly separate from the power-generating function, which

generally has been in the domain of investor-owned utilities.

Many small communities generate their own electricity; but

their electric utility departments are operated separately

from their waste management departments.  Consequently,

unlike the European experience, energy recovery from waste

in the United States has evolved within the waste management

sector; the conventional energy-producing sector has begun

to accept solid waste as an energy source only recently and

rather cautiously.


     Until 1967, all incinerators operating in the United

States were refractory-lined units (a few had waste-heat

boilers, but very little energy was recovered).  The passage

of stricter air pollution control laws in the late 1960's

made refractory-lined incinerators prohibitively expensive

and led to cautious experimentation with waterwall furnaces,

a technology which was already gaining widespread acceptance

in Europe.

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                                                            474




     The first waterwall combustion unit was built in the



United States in 1967 and is owned and operated by the U.S.



Navy at the Norfolk, (Virginia)  Navy Base.  Designed much



like a refractory furnace, except that it is flitted with



water tubes, this unit is a typical of modern waterwall



combustors.








     The first sophisticated U.S. system, patterned after



the European designs, was constructed in 1971 at Braintree,



Massachusetts.  Shortly thereafter, systems were built at



Chicago, Illinois, and at Harrisburg, Pennsylvania, that



utilized the Martin  (Munich, West Germany) design.  Although



all were designed with the possibility of selling the steam,



generated, none of these plants did so until after the 1974



oil embargo.  More recently, however, waterwall combustion



units have been constructed at Nashville, Tennessee, and



Saugus, Massachusetts. Unlike their American predecessors,



markets for the recovered steam  (and chilled water at Nashville)



were secured prior to construction, assuring sale of their



products.  Brief descriptions of these systems are included



in this report.








     A second approach to recovering energy from unprocessed



municipal  solid waste is through the use of small two-



chamber, modular incinerators.  These shop-fabricated units



have been  in widespread use for many years; but only recently



have they  been adapted to heat recovery or municipal operation.

-------
                                                         475

Ranging in size from 1 to 20 tons per day, they were histor-

ically used in industrial, commercial, or institutional

applications.  More recently, they have been used in municipal

operations; by installing multiple units the plants range in
                                              \
capacity from 20 to 100 tons per day.  These units have been

operated as steam producers with the total steam production

being utilized by a single, adjacent industrial facility.

Because they are shop-fabricated, construction is quick and

simple, requiring only a minimum of skilled labor.  Their

capital and operating costs make them feasible in some

instances for communities as small as 10,000 to 15,000

people.  Even smaller communities might find them practical

in situations where a facility can dispose of both municipal

waste and plant waste generated by the steam-using industry.




     At the same time that waterwall combustion technology

was gaining widespread acceptance in Europe, a different

concept was being pursued in the United States.  Whereas the

waterwall concept attempts to design the best possible

combuster to accommodate the difficult fuel called solid

waste, the American concept was to transform the solid waste

into a fuel that could be burned in existing fossil fuel

combustors.  Thus, the European approach adapts the combustor

to the fuel while the American approach adapts the fuel to

the combustor.  This concept is commonly referred to as

"refuse-derived fuel  (RDF)"; the RDF can be burned in a

dedicated spreader-stoker furnace or as a supplement to coal

in a suspension-fired boiler.

                              6

-------
                                                          476




     The concept of direct combustion of solid waste in



combination with a fossil fuel in an existing boiler was



originally proposed in 1968.  The Union Electric Company of



St. Louis, Missouri, encouraged the City of St,. Louis to



apply to the Office of Solid Waste of the EPA for a grant to



demonstrate the use of prepared solid waste as a supplement



to pulverized coal in an existing suspension-fired, steam-



electric boiler.  Construction of the first test facility



was completed in 1972 and evaluations were completed in



1976.  Even before the evaluations were complete, several



other cities began constructing similar facilities.  Plants



are currently in operation in Ames, Iowa; Milwaukee, Wisconsin;



and Baltimore County, Maryland.  Other plants are under



construction in Bridgeport, Connecticut; Chicago, Illinois;



and Monroe County, New York.








     Pyrolysis of municipal solid waste has largely been an



American concept, and it was developed as an effort to



convert solid waste into a more readily marketable fuel.



Ideally, this fuel, produced from solid waste, would be



easily transported to distant users, would be easily stored



for use when needed  (as opposed to having to be used as soon



as it is produced), and would be compatible with other



conventional fuels.  In essence, the fuel user would think



of this fuel as being interchangeable with other fossil



fuels.

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                                                             477
     Efforts to develop this system have met with only
limited success, and consequently, despite 10 years of
extensive developmental activity, the concept is still not
ready for widespread commercial use.  Although there are 50
or more organizations working on different pyrolysis systems,
only 4 have evolved to the "full-scale" demonstration stage.
The largest of these is the 900 tonne  (1,000 ton)-per-day,
rotary-kiln pyrolysis reactor built in Baltimore, Maryland,
with financial assistance from EPA.  Although it has operated
intermittently since 1975, the plant has been plagued with
a number of mechanical problems.  At present, the city of
Baltimore is in the midst of a major program of modifications
in order to improve plant performance.

     Another plant was built with EPA assistance in San
Diego County, California.  This 180 tonne (200 ton)-per-day
facility was designed and built by the Occidental Research
Corporation.  Two other 180 tonne  (200 ton)-per-day plants
are undergoing testing.  One is the Union Carbide test
facility built, owned, and operated by them at their S.
Charleston, West Virginia, industrial complex.  The other
plant is in Luxemburg, where it was built by Andco, Incorporated,
as a commercial facility.  This plant uses the Torrax process,
which was originally developed by the Carborundum Corporation
in Erie County, New York.

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                                                        478
              Mass Burning of Unprocessed Waste
                    Waterwall Combustion
Process Description


     Municipal solid waste is deposited on a tipping floor
or in a large storage pit from which it is transferred to
the furnace feed hopper.  From the feed hopper, the waste is
fed onto mechanical grates, where it burns as it moves con-
tinuously through the furnace.  Noncombustible material
falls off the end of the grate, where it is quenched with
water and then conveyed to trucks or a temporary storage
pit.  Ferrous metal is routinely recovered from the residue,
and in Europe the ash is often used as a road building
material.


     The furnaces are enclosed by closely spaced water-
filled tubes.  Water circulating through the tubes recovers
heat radiated from the burning waste.  Some solid-waste-
fired steam generators employ refractory walls.  Integrally
constructed  (attached) heat recovery boilers generate steam
while reducing the temperature  (and the volume) of the
exhaust gases.  The boilers,consist of various zones or tube
packages referred to as superheaters, economizers, reheaters,
etc., depending upon the function of the particular zone.
A marketable product  (steam)  is created while permitting the
use of smaller gas-cleaning equipment  (gas volume is pro-
portional to absolute temperature).

-------
                                                         479

     In the combustion process, oxygen  (air) is required to


burn the fuel and release heat.  Air is introduced above and

below the fuel bed  (overfire air-underfire air) to promote

mixing of the gases  (turbulence) and to complete combustion
                                              \
in the furnace.  The combustion gases, after being cooled

as they pass through the various boiler sections are passed

through air pollution control devices  (generally electrostatic

precipitators) and are then vented to the atmosphere through

a stack.




Status of Major Projects




     Braintree, Massachusetts.  In September 1971, the Town

of Braintree began to operate its two independent waterwall

furnaces equipped with Riley traveling grates.  The furnaces

were constructed by Antonellis-Pyro Furnace Contractors.

Each furnace is designed to burn 108 tonnes  (120 tons) per

day of municipal solid waste with a higher heating value of

11.5 kilojoules per kilogram  (5,000 British thermal units

per pound).  The solid waste is not processed before combustion,




     The plant's two steam generating boilers are designed

to produce a total of 27,000 kg (60,000 Ibs) per hour of

steam at 1,700 kPa  (250 pounds per square inch gauge).


Actual, output of steam is somewhat lower—23,000 to 25,000

kg/hr (52,000 to 56,000 Ib/hr) because of condenser capacity

limitations.
                              10

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                                                       480




     The plant was built at an initial cost of $2.5 million,



excluding land.  However, the plant has recently undergone



extensive rebuilding, including replacement of the original



electrostatic precipatator with new high efficiency units.








     Chicago (Northwest), Illinois.  In December 1971, the



City of Chicago began to operate its northwest plant, which



has four independent waterwall furnaces with Martin reverse



reciprocating grates.  Each of the four furnaces is designed



to burn 360 tonnes (400 tons) per 24-hour day.  Three units



are always in use; one is reserved for standby capacity.



The plant was built at a cost of $23 million, including



land.








     A shredder was installed to reduce oversized bulky



waste, but it has not been used because of excessive amounts



of dust and noise.   (The shredder would have been powered by



steam generated on-site.)  Consequently, no solid waste is



processed prior to combustion.








     The plant's four steam-generating boilers are designed



to produce a total of 198,000 kg/hr of steam at 1,700 kPa



 (440,000 Ibs/hr at 250 psig-) .  Some of the steam is used to



heat the maintenance garage; the rest was condensed.  In



addition, a steam line to a nearby industrial customer is



being installed, and steam sales are anticipated to start in



1979.
                               11

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                                                            481
     All four furnaces have electrostatic precipitators to
control particulate emissions.  Fly ash, bottom residue, and
grate siftings are dropped into a quench trough and are
conveyed to a separate building.


     Harrisburg, Pennsylvania.  The city of Harrisburg's
waterwall combustion unit was completed in June 1972.  Its
two independent waterwall furnaces have Martin reverse
reciprocating grates and boilers designed by the IBW-Martin
Group.  Each furnace is designed to burn 324 tonnes  (360
tons) per 24-hour day, 5 days per week.  A shredder reduces
oversized bulky wastes to particles of less than 15 cm  (6
in.).  The shredder is driven by steam generated on-site.
There is no other pretreatment of the solid waste.


     The plant's two steam-generating boilers are designed
to produce a total of 108,000 kg/hr of steam at 2000 kPa
(240,000 Ibs/hr at 300 psig).  About 20 percent of the steam
is used to heat the building and maintenance garage and to
power the shredder.  A 2-mile steam line was completed in
1978 to tie this plant into an existing downtown steam loop.
Sales of steam started in late 1978.


     In addition, the Harrisburg plant is being modified to
burn dryed sewage sludge along with the solid waste.  Sludge
from a wastewater treatment plant at 5 percent solids will
be pumped to the waterwall combustion unit where it will be
                               12

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                                                       48^
dewatered in vacuum filters to 20 percent solids and then
dried to 10 percent moisture in a steam-heated "porcupine"
dryer.  The dry sludge will then be introduced into the
furnace and burned.


     The two furnaces have electrostatic precipitators to
control particulate emissions.  Fly ash, bottom ash residue,
and grate siftings are dropped into a quench tank and conveyed
under a magnet to a storage hopper for loading into trucks,
which haul the residue to an adjacent site.  Magnetically
separated ferrous metals are being sold to a local scrap
dealer.


     The plant was built at a cost of $8.3 million, excluding
land, new steam line, and sludge systems.


     Nashville, Tennessee.  The Nashville Thermal Transfer
Corporation, a nonprofit authority created by the State of
Tennessee, began operating the facility in June 1974.
Unlike other installations, the system was originally conceived
as a fossil-fuel-fired district heating and cooling system.

Later, but still in the planning stages, it was decided to
use solid waste instead of fossil fuel as the primary energy
source.
                               13

-------
                                                            483
     The two furnaces are equipped with Detroit Stoker
Company agitating grates and each is designed to burn 324
tonnes  (360 tons) per 24-hour day.  Eventually, the plant
will be expanded to include one additional 324-tonne (360
ton) unit.  A package-type boiler, which can be fired by oil
or gas, serves in a standby capacity.  This is necessary
because some of Thermal's customers have no alternative
means of heating or cooling their buildings.

     The boilers are designed to produce a total of 177,750
kg/hr of steam at 3,000 kPa  (395,000 Ibs/hr at 400 psig).
Heat is distributed directly as 316-C  (600 F) steam.  For
cooling, steam turbine-driven chillers, rated at 12,600
tonnes  (14,000 tons) of cooling capacity, provide water at 5
C  (41 F) for piping to customers.

     The two furnaces were originally equipped with low-
energy scrubbers (water spray chambers).  This equipment
controlled particulate emissions to a level of 0.19 grains
per cubic foot (corrected to 12 percent carbon dioxide);
this is significantly higher than the Federal New Source
Performance Standard of 0.08 gr/scf.  Consequently, the
corporation had to replace the scrubbers with electrostatic
precipitators. The new units have been found to maintain
emissions at 0.024 gr/scf, well below the Federal standard.
                              14

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                                                       484
     Saugus, Massachusetts.  RESCO, Incorporated, a joint
venture of Wheelabrator-Frye, Incorporated (the U.S. licensee
of the Von Roll incinerator), and a local construction and
landfill company, is now operating a facility designed to
burn 1,100 tonnes (1,200 tons) per 24-hour day of solid
waste.  In operation since April 1975, the facility produces'
steam for a large General Electric Company industrial plant
for use in processing, power generation, and testing of
steam turbines and jet engines produced at the plant.


     Two 540-tonne (600 ton) furnaces of Von Roll design
generate steam at the rate of 83.9 t/hr  (185,000 Ibs/hr)
each.  Total maximum demand is 158.7 t/hr  (350,000 Ibs/hr);
average demand is 102.0 to 113.4 t/hr  (225,000 to 250,000
Ibs/hr).  Steam is used at three different pressures:
10,342.5, 4,481.8, and 1,379.0 kPa  (1,500, 650, and 200
psig).


     Oceanside, New York.  This 750-TPD plant was built in
1965.  It originally had three batch-feed refractory furnaces,
two with waste-heat boilers.  The two units with heat recovery
have been replaced with waterwall units with continuous
feed.  The saturated steam ,is ude for in-plant electricity
generation.  The plant uses electrostatic precipitators as
the emissions control devices and is meeting required standards,
                               15

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                                                          435



     Hampton, Virginia.  This 400-TPD unit is under construction.



It will consist of two 200-TPD furnaces and will supply



steam for a Federal government complex.








         Small Two-Chamber, Modular Combustion Units








     The use of small modular combustion units as a means of



recovering energy from municipal solid waste is an excellent



example of modifing and adapting an established technology



to a new prupose.  Virtually thousands of these units exist



in the United States where some 20 companies manufacture



them.  Their greatest use in the past has been exclusively



for volume reduction—generally in large retail or commercial



complexes, apartment houses, institutions, and industrial



sites.  The addition of heat-recovery units to recover



energy either as hot water, steam, or heated air has only



been incorporated during the past few years.  There are



currently about 20 such heat-recovery units in operation and



most of these are in industrial sites.  The several municipal



operations range in size from 15 to 100 tonnes-per-day



capacity.  At least one industrial site is burning municipal



waste 1 day a week and industrial waste during the remaining



time.
                              16

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                                                         486
Process Description
     A key objective of this type of system is to keep the
total capital cost as low as possible and the systems as
simple as possible, from a viewpoint of design, construction,
operation, and maintenance.  The units are shop fabricated
and shipped to the site ready for placement on a concrete
foundation.  All instrumentation and controls are ussually
installed at the factory.


     The facility is typically a preengineered metal-skinned
building enclosing a concrete pad.  Waste is simply dumped
on the pad and then pushed by a small front-end loader into
a hydraulically operated ram-feeder.  The front-eiid loader
operator typically serves as the plant operator.  Thermocouples
inside the primary combustion chamber automatically control
the cycling of the ram feeder.  While designs vary among
manufacturers, the two-chamber, starved-air incinerator
appears to be the most popular unit for heat recovery.  In
this type of unit the primary chamber accepts waste on a
refractory floor equipped with air pipes and burns the waste
on an unagitated fixed bed.  The units are frequently operated
substoichiometrically which results in the pyrolysis of the
feed stock.  They operate as a fixed-bed pyrolysis system
because air is fed into the bottom of the fuel bed through a
bed of ash, charcoal, and fresh fuel, where the products of
combustion devolatilize the raw waste and exit the primary
                              17

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                                                       487



chamber.  The off-gases are consumed in an afterburner,



where they are mixed with air and ignited.  Normally, some



fossil fuel is burned to sustain the afterburner temperature



because the heating value of the primary chamber off-gas is



too low to sustain combustion.  The afterburner is generally



the only air pollution control device employed in these



units.  The hot products of combustion from the afterburner



are passed through a heat exchanger to generate hot air,



water, or steam.  These units are prevalent because of



mechanical simplicity and low cost.  They also have inherently



low fly ash emission characteristics, which lend them to



serving as a heat exchanger heat source withour undue fouling



potential.  The ash is frequently allowed to accumulate



until the unit is full and then the unit is cooled and



manually de-ashed.  Modern units employ ash-handling systems



of various designs, including an air-lock guillotine door



opposite the feed opening and a secondary ram which advances



the ash into a closed, spray-equipped ash discharge hopper



incorporating a water spray dust suppressions system.







Status








     Blytheville, Arkansas.,  This is the first small modular



combustion unit to burn municipal solid waste for energy



recovery.  As such it has experienced numerous problems



typical of a first generation plant.  The plant is 4 years



old and consists of four Consumat starved-air furnaces with
                              18

-------
                                                         480




a total capacity of 45 tonnes (50 tons) per day.   Built at



an initial cost of $800,000, it operates 10 hours per day



and supplies 24,000 pounds of steam per day to a  nearby



chrome-plating industry.








     Groveton, New Hampshire.  This unit was purchased in



1975 by the Groveton Paper Products Division of Diamond



International at a cost of $250,000 and is designed to



handle 27 tonnes (30 tons) of mill waste and municipal solid



waste per day.  This unit,, built by the Environmental Control



Products Corporation, has automatic ash removal,  allowing



continuous operation.  The unit burns primarily dirt from



the papermill's wood chip feedstock; mill waste;  and, 1 day



per week, the waste collected from the town's 1,600 residents



The unit provides 4,000 to 6,000 pounds of steam per hour—a



small percentage of the plant's total steam load.








     Siloam Springs, Arkansas.  The plant consists of two



Consumat units with a combined capacity of 18 tonnes  (20



tons) per day.  Like Blytheville, this plant does not have



automatic ash removal so it can be operated only until the



ash depth builds up to a certain point.  Thus, a 24-hour



operating cycle consists of 10 hours of burning followed by



burndown, cooldown, and ash removal.  The plant has operated



with a minimum of maintenance expense.
                               19

-------
                                                        489
     The plant was built in 1975 at a total capital cost of
$375,000.  Four thousand five hundred (4,500)  pounds of
steam per hour are supplied to an adjacent canning plant.


     North Little Rock, Arkansas.  This plant began operating
in September 1977 and, in addition to being the newest heat-
recovery modular combustion unit, it is also the largest.
The plant has a total capacity of 90 tonnes (100 tons) per
day.  Four combustion units serve two waste-heat boilers.
Total steam output is 15,000 pounds per hour at 750 to 790
kPa  (110 to 115 psig).  The plant is located on the property
of a creosoting plant which uses the steam.  The facility
cost, excluding land, was approximately $1.5 million.


     Crossville, Tennessee.  This 60-TPD plant went into
operation in 1978 and supplies steam to a rubber-tire plant.
In addition to municipal solid waste, this plant burns some
scrap rubber.  The two continuous-feed units were supplied
by the Farrier Corporation.


     Salem, Virginia.  This is a 100-TPD plant based on the
design at North Little Rock.  The plant started operation in
late 1978 and is basically a later version of the units in
Arkansas.


     Genesee County, Michigan.  This 100-TPD plant is under
construction.  The two 50-TPD units are being supplied by
Consumat.  These units, at 2 TPD, are the largest built to
date.                         20

-------
                                                             49O




            Mechanical Processing of Solid Waste








                     Refuse-Derived Fuel








Process Description








     The production of refuse-derived fuel can be done in



many different ways and most plants built to date exhibit



different philosophies as to design.  In general, however,



the process entails primary shredding to reduce the nominal



particle size of the waste to about 10 cm  (4 inches).  At



this point, ferrous metal is usually removed and the remaining



material is separated into a lighter, mostly combustible



fraction and a heavier, mostly noncombustible fraction.



This separation is done using an "air classifier" in which



the shredded waste stream is injected into a strong, vertically



rising airstream.  Lighter materials are carried up through



the device by the air current.  Heavier materials are pulled



by gravity down through the airstream where they drop from



the bottom of the classifier.  The light fraction is then



further processed to improve its fuel characteristics.  This



further processing generally consists of a second shredding



step but can also entail screening to remove fine inorganic



particles.  Modified supplementary fuels can also be produced



by treating the organics with a chemical embrittling agent



and then grinding them to a powder-like consistency or by



densifying the organics in a pellet mill.  This  latter



variation then produces a small, dense fuel pellet very




                              21

-------
                                                            491
similar to coal nuggets which are suitable as a fuel in a
stoker-fired boiler equipped with a grate.

     The RDF that is produced can be burned as a supplement
to coal or can be burned in a dedicated spreader-stoker
boiler as a primary fuel.  Both approaches are being implemented.
This technology, although new, does have application, and as
more systems are implemented the technical uncertainties of
the processing and combustion systems can be reduced, eliminated,
or at least identified.

Status of Major Projects

     St. Louis, Missouri.  Although this test facility is no
longer in operation, it is important to review the experience
gained since the facility served as a model for most of the
later implementations.  Therefore, the results of this
project will be discussed in greater detail.

     The city of St. Louis, Missouri, with demonstration
grant support from the Office of Solid Waste, U.S. Environmental
Protection Agency, and with the cooperation and investment
of the Union Electric Company, began preparing solid waste
for use as a supplementary boiler fuel in April 1972.  The
plant was closed for extensive modifications from May to
November 1973 and was shut down permanently in 1976, following
completion of the evalution program.
                              22

-------
                                                          49Z




     Design Capacity.   The plant was designed to process 270



tonnes (300 tons)  per operating day.  Processing was con-



fined to one 8-hour-shift per day with firing into the



boiler on a 24-hour-per-day basis.  The processing line was



designed to handle 40.5 tonnes (45 tons) per hour and included



a shredder for size reduction, an air classifier to separate



the fuel fraction, a magnet to separate ferrous metals, and



a densifier to upgrade the quality of the ferrous product.



As would be expected of a prototype, the facility encountered



many operating problems.  In addition, the plant had only



one processing line and no redundancy.  However, the plant



processed about 52,000 tonnes (60,000 tons) of waste



throughout the demonstration period.  The plant normally



processed 135 tonnes  (150 tons)  per day when the power plant



could accept waste on a 24-hour basis.








     Waste Characteristics.  An1analysis of the input waste



streams, on the average indicates the following:








     As received  (wet weight) Basis








     Heating value            10.0  MJ/kg  (4675 Btu/lb)



     Moisture content         30    percent



     Sulfur                    0.11 percent



     Chlorine                  0.33 percent



     Sodium Chloride           1.27 percent



     Ash                      20    percent
                               23

-------
                                                          493*


     Only residential wastes were processed at the facility.




     Products.  The air classified fuel fraction represented

about 74 percent of the input waste.   About 98 percent of

the fuel was less than 3.15 cm (1.5 inches) in size (any

dimension).  Analysis of the fuel fraction, on the average,


indicated the following:




     As Fired (wet weight) Basis




     Heating value            11.6  MJ/kg  (5,006 Btu/lb)


     Moisture                 27.5  percent

     Sulfur                    0.11 percent

     Chlorine                  0.34 percent

     Sodium Chloride           0.27 percent

     Ash                      18.5  percent




     Power Plant Experience.  Test firing rates at the power

plant varied from 5 to 27 percent of the total heat load of

the boiler.  However, because the RDF was not fired con-

tinuously, the RDF provided only 3 percent of the heat input

to the boiler over the life of the project.  There was no
                                                •
measurable physical effect of the RDF on the boiler.

Bottom ash did increase significantly, but did not exceed

the capability of the existing bottom-ash handling equipment.


A major maintenance problem was found to be abrasive wearing

of the elbows in the pnuematic transport lines.  This prob-

lem was addressed by additional processing of the waste


                              24

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                                                         494
stream to reduce the inorganics and by installing abrasive
resistant wear plates in the critical locations.

     Particulate emissions were found to increase when RDF
was burned with coal, but only when the boiler was operating
at its maximum capacity of 140 megawatts (MW).  At its
design capacity of 125 MW, there was no significant change.
It is felt that at the larger boiler load the design capacity
of the electrostatic precipitator was exceeded. This is a
site-specific phenomenon which is a function of the actual
capacities of the various system components, and as such
cannot be used to predict the performance of any other
system.

     Ames, Iowa.  This municipally owned facility is the
first commercial RDF plant to be built.  It was patterned
after the St. Louis demonstration facility.  The plant,
which has been operating since November 1975, was built at a
cost of $5.6 million and is designed to process 36 tonnes
 (40 tons) of waste per hour.  However, the plant has required
about 7 hours to process the 150 tons of waste brought to
the plant each day.  In this facility two stages of shredding
precede the air classification step, recovering about 80
percent of this incoming waste as 4 cm  (1 1/2  inch) fluff
RDF.  The RDF is transported pnuematically to  the adjacent,
city-owned power plant.  The power plant is outfitted with a
small  (33 MW) suspension-fired boiler and two  20 MW spreader-
stoker  (grate-equipped) boilers.  It has been  found that the
                               25

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                                                        495



suspension fired boiler is too small to provide sufficient



retention time for the heavier organic particles to completely



combust.  Because of this the city has been burning the RDF



in less efficient stoker-fired units.  These units have been



able to burn RDF at rates up to 50 percent  (on a heat-input-



basis).  However, these units are not as efficient as the



suspension-fired boiler so it power plant incurs an economic



penalty by using them instead of the suspension-fired unit.



Therefore, the city is installing a burnout grate in the



suspension-fired unit so it can go back to the more efficient



boiler.








     Milwaukee,Wisconsin.  This RDF facility is owned and



operated by the Americology Division of American Can Company



under contract to the city of Milwaukee.  The 1,100-tonnes



(1,200 tons)-per-day facility was built at a reported cost



of approximately $18 million, including $4 million in modifi-



cations at the Wisconsin Electric Power Company power plant.



Waste is first shredded to 10 cm  (4 inches) and then separated



in a zig-zag air classifier.  The light fraction representing



about 60 percent of the input waste stream is then reshredded



to about 4 cm  (1 1/2 inches).  The RDF is transported to the



power plant in 57-cu m (75 cubic yard) transfer trailers.








     The plant has been in operation for about 1 year and is



currently processing about 600 tons per day.  The RDF is



being burned in a 300 MW suspension-fired boiler.  Inexplicably,



the fuel product has been of much lower qulaity than expected.



                              26

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                                                              496
Ash content has been 33 percent and moisture has been running
34 percent.  As a consequence/ they have experienced severe
slagging in the boiler.  Americology is modifying the processing
plant in an effort to improve the quality of the RDF.


     The following plants are under construction or in
various stages of start-up.


     Chicago, Illinois.  This 1,000 TPD plant, which consists
of two processing lines, will produce an RDF product that
can be used supplement coal at Commonwealth Edison's Crawford
electric generating plant.


     Bridgeport, Connecticut.  The plant is to process 1,800
TPD into a powdered RDF  (Eco-Fuel II) in a proprietary
process that uses a special embrittlement agent and a heated
ball-mill pulverizer.  The powdered RDF will be burned to
supplement oil at United Illuminating1s Devon electric
generating plant.


     Lane County  (Eugene), Oregon.  This small 500-TPD plant
has a single processing line.  The RDF will be used to
supplement wood waste  (hog fuel) at a local site.


     Monroe County, New York.  This 2,000-TPD plant has two
processing lines.  The RDF will be burned as a supplement to
coal in Rochester Gas and Electric's No. 7 plant.
                              27

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                                                        497


     In addition to the supplemental fuel systems listed


above, RDF is being used as a primary fuel in a number of


locations.  These plants, all of which are under construction


or in start-up prepare the waste by shredding, some air


classification, magnetic metals removal, and screening, and


burn the predominantly organic material in a hog-fuel type


boiler with a grate to produce steam.  Normally, the shredded


waste  (coarse RDF) is the only fuel, but a few plants are


under design that plan a 50-50 mixture of coal and coarse


RDF.  The fuel can also be produced by wet pulping, as


developed in the EPA-supported demonstration project in


Franklin, Ohio.  This approach is being implemented in


Hempstead.  Two processing lines feeding two boilers are


typical.






     Akron, Ohio^  This 1,000-TPD'plant will employ two


processing lines to produce a coarse RDF that will be burned


in two spreader-stoker boilers.  The superheated steam will


be used for urban and industrial heating.






     Albany, New York.  The RDF at this 750-TPD facility


will be prepared and shipped across the city to a spreader-


stoker boiler suppling heating steam to a number of State


office buildings.






     Niagara Falls, New York.  This system is privately


owned and operated and will be supplying steam to the Hooker


Chemical Company.  The solid waste will come from the communities


in the vicinity of the plant.
                               2 8

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                                                       498
     Hempstead, New York.  This 2,000 TPD plant uses the wet
separation process to produce RDF.  The fuel, after dewatering
to 50 percent moisture, is combusted in a boiler and the
superheated steam generated is used to produce electricity
which is sold into the grid.  The plant is beginning operations
and is now at half capacity.  A sister plant will be built
in Dade County, Florida.

                      Pyrolysis Systems

     Pyrolysis is the destructive distillation of the organic
fraction of solid waste.  It occurs when organic material is
exposed to heat in the absence or near absence of oxygen.
Pyrolysis differs from combustion in that it is endothermic
(heat absorbing) rather thari exothermic.  Processes under
development use heat from part of the waste to provide the
heat absorbed during pyrolysis and recover the remaining
heat in the form of steam or a gaseous or liquid fuel.

     All processes reduce the solid waste to three forms:
gases  (primarily hydrogen, methane, carbon monoxide, and
carbon dioxide); liquids  (water and organic chemicals,  such
as acetic acid, methanol, and benzene); and solids  (a
carbonaceous char).  The form and characteristics of the
fuel fraction varies for each of the different processes
under development and  is a  function of the reaction time,
temperature and pressure in the pyrolysis reactor, the
particle size of the feed,  and the presence of catalysts.
                                29

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                                                          499



     To maximize gas production, reactor temperatures are



held in the range of 800 C to 1,600 C (1,400 F'to 3,000 F) ;



for oil, temperature is on the order of 500 C (900 F).



Pressures range from 1 to 70 atmospheres.  Ideally, the



reaction is allowed to take place in the absence of diluting



gases so that the product is the volatile matter of the



solid waste.  If air is used in the reactor, the gases



produced will be diluted by the nitrogen in the air  (air is



approximately 79 percent nitrogen and 21 percent oxygen).



As a result, some processes have been developed which use



oxygen/ thus resulting in a higher heat-content fuel gas.



Other systems indirectly transfer the heat to the gasifier



to minimize dilution of the product gas.








     Heating solid waste releases gases and leaves a carbon



residue called char.  In some reactors, the residue reaches



such high temperatures that the ash and other noncombustibles,



such as cans and glass, melt to form a slag, which can be



removed from the reactor in a molten state and quenched to



form a glassy aggregate.








     Residues produced from pyrolysis are biologically



inactive and may be safely -disposed in sanitary landfills.



Solid residues from the noncombustible portions of the



refuse, such as glassy aggregate, may be used for construc-



tion and paving.  If the char is not consumed in the process,



it has a higher heating value of approximately 10 MJ/kg



(9,000 Btu/lb).  Its high ash content (50 percent), however,



                              30

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                                                             oCO
severely limits its usefulness.  Clearly,  failure to consume
all the char in the process represents a loss in energy
recovery.


     This paper describes the four pyrolysis systems, which
can be classified as "developmental."  There are presently
no commercially operational pyrolysis systems, and there are
numerous other systems which can be considered "experimental."
All four of the systems described have been previously
operated on a small pilot scale.  Full-sized plants of 200
tons per day or larger are currently being tested.  Two of
the systems produce low energy gas which is used "on-site"
to produce steam.  The third system produces a medium-energy
gas which can be sold to a nearby industrial user or may be
suitable as a chemical feedstock.  The fourth system pro-
duces an oil-like liquid fuel which can be stored and
transported for use "off-site" in large industrial or
utility boilers.


     Baltimore, Maryland.  The 1,000-TPD pyrolysis plant
currently in operation  in Baltimore, Maryland, was originally
developed by Monsanto Enviro-Chem Systems, Incorporated.
The process involves a starved-air primary furnace chamber
 (pyrolyzer) and immediate combustion of the low-heat value
gases in an afterburner for recovery of heat.  Waste is
shredded, conveyed to a storage silo, and subsequently fed
to a rotary kiln where it is pyrolyzed.  Fuel oil is also
burned in the kiln to provide  some of the heat for the
                               31

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                                                      501




pyrolysis reaction.  The burner is arranged to provide a



counter current flow of gases and solids, thus exposing the



waste to progressively higher temperatures as it passes



through the kiln.  The finished residue is exposed to the



highest temperature, 1,000 C (1,800 F), just before it is



discharged from the kiln and quenched in a water-filled



tank.  The residuals were to.be split into three fractions:



glassy aggregate, ferrous, and char.  The glassy aggregate



and ferrous materials were to be recovered for sale and the



char was to be dewatered and landfilled.








     Gases resulting from the pyrolysis reaction have a high



temperature and low heating value  (making off-site trans-



portation uneconomical); therefore, they are immediately



mixed with air and burned in an afterburner to liberate the



heat of combustion.  The gases then pass through waste-heat



boilers where steam is generated for distribution.  Steam is



produced at 213 C  (415 F) and 1,400 to  3,600 Kg/cm2  (100 to



260 psi) pressure.








     Status.  Construction of the plant was completed in



February 1975 under a turnkey contract with Monsanto.



However, normal operation of. the plant has not been possible



because a number of process changes were needed in order to



ensure proper operation.  These changes are currently being



made and are expected to be completed in early 1979.
                              32

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                                                            502



     As originally built, exhaust gases were cleaned by



means of a large spray tower.  Initial tests of the spray



tower showed that it could not clean the gases sufficiently



to meet the required ordinances.   All efforts to modify the



plant to meet the standard have failed, and as a result it



has been decided to replace the low energy scrubbers with



dry, electrostatic precipitators.  Other problem areas that



have required modification or have not worked completely as



intended include:  blockage in the shredded-waste storage



bin and hydraulic ram feeder to the kiln; loss of refractory



lining in the kiln and afterburner due to slagging and



temperature control problems; excessive vibration in the



induced draft fan; and failure of the residue drag conveyor.



Most of these other problems have now been eliminated or



reduced.








     Although Monsanto is no longer associated with the



project, the city of Baltimore has proceeded with the



modifications.  The original cost of the plant was $16



million, excluding land.  With the modifications currently



underway, the total cost of the plant will rise to about $25



million.








     The city has continued to operate the plant while the



modifications have been  underway.  During the first 8 months



of  1977, 54,000 tonnes  (60,000 tons) of  solid waste were



processed.  From this waste  225 million  pounds of  steam were
                               33

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                                                      503

produced and sold to the Baltimore Gas and Electric Company

for $680,000.




     San Diego County, California.  A 180-tonnes (200 tons)-
                                              \
per-day pilot plant was built under a turnkey contract by

the Occidental Research Corporation.  This process was to

convert the organic portion of the waste into an oil-like

liquid fuel that could be used as a substitute for No. 6

fuel oil.  Pyrolysis of the organic material occurs almost

instantaneously because it is mixed turbulently with hot

glowing char in an inert atmosphere.  The concept was originally

tested in a small laboratory unit.  In 1971, a 3.6-TPD  (4

TPD) pilot plant was built by Occidental at LaVerne, California.

Successful laboratory scale testing has since led San Diego

County, California, and EPA to fund the 180-TPD  (200 TPD)

demonstration plant.




     In order for this flash pyrolysis process to work

efficiently, most inorganic materials must be removed and

the organic materials must be reduced to small, dry particles.

Incoming municipal solid waste was first shredded to a

particle size of 5 cm (2 inches) or less.  An air classifier

then separated the light, organic fraction from the heavy,

inorganic fraction.  The "lights" were dried to a moisture

content of 3 percent.  A screen removed additional inorganics,

and the remaining material was shredded again to a particle

size of -14 mesh. The material must pass through a screen

having 1.81 mm openings  (14 openings per inch).  Ferrous

                              34

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                                                        504




metals were reclaimed magnetically from the classifier



rejects; and a sandlike, mixed-color, glass cullet of 99.7-




percent purity was recovered from the remaining inorganics



by selective crushing and screening, followed by froth




flotation.








     The pyrolysis reaction took place in a transport




reactor 9.14-m tall and 20 cm in diameter  (30-feet tall and



8 inches in diameter).  The fine-shredded material was




carried into the base of the reactor where it was mixed with



burning char.  Both materials were carried through the




system by spent combustion gases from an auxiliary char



burner.  In the reactor, the hot, glowing char and solid



waste mixes rapidly as the material passes upward under




turbulent flow conditions.  Reactor temperature were main-



tained, without any auxiliary fuel, at about 480 C (900 F).




Because the pyrolysis reaction was so rapid, the gaseous



products formed are not exposed to the high temperatures




long enough for them to degrade thermally.  The result is



that when the gases are cooled down to ambient temperatures,



the compounds formed are organic liquids rather than gases.








     After removal of char by cyclones, the hot gases passed




to a standard oil-recovery collection train.  Hot char could




either be recirculated to the pyrolysis reactor after being




reheated in the char heater, or quenched for disposal.
                               35

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                                                        505

     The hot,  char-free gaseous products leaving the reactor

cyclone were cooled rapidly, from about 480 C '(9OF)  to 65 C

(150F) by a venturi quench system using recirculated product

oil.  In this way, the liquid products, at the rate of about
      3                                       \
0.14 m  (0.9 barrel or 36 gal) per ton of solid waste, were

recovered before thermal cracking could occur.  The outlet

gas was cooled further to 43 C (110 F) in a packed-bed

scrubber before being returned to the process. Condensed

water from the decomposition of cellulosic compounds amounted

to about 13 percent of the pyrolysis feed.  This water was

cooled in a separate heat exchanger, and a portion was then

returned to the scrubber for cooling purposes.



     The liquid fuel obtained from the pyrolysis of municipal

refuse differs in many important aspects from fuel oil

derived from petroleum.  It is a complex, highly oxygenated

organic fluid.  The sulfur content is a good deal lower than

that of even the best-residued oils.  To produce the same

amount of energy as No. 6 fuel oil, nearly twice its weight

in pyrolytic oil would be needed; the average heating value

of pyrolytic oil is about 5,000 kJ/kg  (10,500 Btu per pound),

compared with 8,640 kJ/kg (18,200 Btu per pound) for a

typical No. 6.  On a volume basis, however, a liter  (or

barrel) of oil derived from the pyrolysis of municipal waste

contains about 76 percent of the heat energy available from

No. 6 fuel oil.
                               36

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                                                           506
     Status.  Construction of the 180 tonnes (200 tons)-per-
day plant was completed in February 1977.  Startup operations
were underway for almost 1 year when it became apparent that
the process would not work as designed and extensive modifications
would be required.  The "front end" of the plant worked
reasonably well, but from the secondary shredder and dryer
on through the pyrolysis system, numerous mechanical and
thermal problems arose.  Reducing and drying the shredded
solid waste to -14 mesh proved very difficult.  The material
was abrasive and equipment life was severely limited. The
pyrolysis reactor and associated hardware did not perform as
designed, and consequently, the little pyrolysis oil that
was produced did not meet the expectations of the operators.
None of this oil was burned in the oil-fired electric utility.
boiler as was originally planned.  At present, the plant is
shut down.  Occidental Research is analyzing the data gathered
during the short runs and will determine the viability of
further modifications.  Until Occidental can assertain the
cost and extent of the modifications required the commerical
viability of this process is questionable.

Souch Charleston, West Virginia.  The Linde Division of the
Union Carbide Corporation has developed a high-temperature
pyrolysis reactor  (called  "Purox") which produces a  fuel gas
that can be recovered for off-site use.  Original pilot-
plant work was done  in Tarrytown, New York, on a  3-m (10
foot) tall, packed-column  retort having  a capacity of  4.5
TPD  (5 TPD).  Union  Carbide is  currently testing  a 180-TPD
                               37

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                                                        507

 (200 TPD)-facility at South Charleston, West Virginia.  This

company-owned test facility is being used to confirm engineering

scale-up criteria, to obtain operating data on and experience

in working with municipal solid waste, and to confirm projected

economics.  In addition to municipal solid waste, separate

tests have been conducted on a mixture of sewage sludge and

solid waste.



     The basic part of the Purox system is a vertical shaft

furnace into which shredded solid waste is charged at the

top.  This furnace operates at atmospheric pressure with

oxygen admitted into the combustion zone at the bottom of

the furnace.  Combustion occurs at the base of the furnace,

and the temperature levels at that point are about 165 C

 (3,000 F).  At this temperature, glass and metal constituents

of the solid waste are fused into a molten slag, the slag

being discharged continuously from the bottom of the furnace

through a water seal.  The furnace temperatures drop off

rapidly above the bottom zone, and the oxidizing conditions

at the bottom of the furnace are replaced by reducing con-

ditions in the middle and upper zones.  In the middle and

upper zones of the furnace, low-temperature distillation and

drying occur together with the reactions between steam and

carbon monoxide and the combustible components of the solid

waste.  The end result of the chemical reactions taking

place in this part of the furnace is the formation of a gas

at a temperature level of about 90 C  (200 F) which has a
                               3
heating value of about 8.9 kJ/m  (300 Btu per cubic foot).

                              38

-------
                                                         508
This gas contains, on a dry basis,  about 50 percent carbon
monoxide, 15 percent carbon dioxide,  and 30 percent hydrogen.


     The gas leaving the furnace contains a large amount of
water-soluble products of pyrolysis.   A standard design
electrostatic precipitator removes  the oil and fly ash,
which are recycled back to the furnace combustion zone.
Following the electrostatic precipitator, a condenser
removes most of the water vapor together with water soluble
components of the gas.  There is very little fly ash in the
product gas because of the electrostatic precipitator, the
filtering action of the refuse bed, and the low gas velocity
in the furnace.  The last condition is accomplished by the
use of oxygen rather than air for the combustion process.
The gas also contains few oxides of nitrogen because the
combustion occurs mostly under reducing conditions and also
because in using oxygen instead of  air, there is very little
nitrogen present in the furnace.


     The Union Carbide Corporation envisions the use of
product gas as a fuel gas.  They indicated that, although
the heating value of the gas is lower than natural gas, the
flame temperature will be higher, based on the heat released
per volume of combustion product.  The lower heating value
is a problem only if the gas must be transported a significant
distance.
                                 39

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                                                         503



     The Purox system, as described by Union Carbide,  will



include the pyrolysis furnace,  the electrostatic precipitator,



the water condenser, and the cryogenic oxygen plant supplying



the pyrolysis furnace.  A flare burner would also be provided



to dispose of the gas and to allow for continuous operation



of the furnace, if the downstream processing unit should be



shut down for some reason.  The gas stream would need to



pass through the hydrogen sulfide and chloride scrubbing



units before being flared, in order to minimize air quality



impacts.  A major support system required as part of the



process is a waste water treatment plant to treat the highly



contaminated waste waters produced in the gas cleanup train.








Torrax Process








     The Torrax process was originally developed by the



Carborundum Company through an EPA demonstration grant to



Erie County, New York.  The process was subsequently sold to



the Andco Corporation who is currently promoting the process



in Europe.  A 180-tonne  (200 ton)-per-day commercial facility



is presently operating in Luxemburg.








     This process is similar to the Union Carbide one in



that pyrolysis takes place in a high-temperature, packed-



bed, vertical shaft reactor.  The major difference, however,



is that preheated air is used in the lower combustion zone



instead of oxygen.  Because of this, the resultant fuel gas
                               40

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                                                        510



is diluted by the nitrogen in the air and thus does not have



as high a heating value.  Consequently,  the gas must be



burned on-site and the energy recovered  as steam.








     The solid waste is charged as received from the solid



waste pit into the gasifier.  The gasifier is a vertical



shaft furnace designed so -that the descending refuse burden



and the ascending high-temperature gases become a counter-



current heat exchanger.  The uppermost portion of the



descending solid waste serves as a plug to minimize the



infiltration of ambient air.  As the solid waste descend,



four distinct process changes occur.  The first is drying,



where the moisture is driven off; the second is pyrolysis,



due to the heat transfer from the ascending hot gases to the



solid waste; the third is combustion in the hearth, where



the carbonaceous char is oxidized to carbon monoxide and



carbon dioxide; and the final process change is melting of



the inert fraction of the solid waste.








     The heat for pyrolyzing and drying the solid waste and



for melting the inert fraction is produced by the combustion



of the carbon char with 1,000 C  (2,000 F) preheated air



supplied to the hearth zone of the gasifier.  The heat thus



generated melts the inerts to form a molten slag, which is



drained continuously through a sealed slag tap  into a water-



quench tank to produce a black,  sterile,  granulated residue.
                               41

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                                                            511




The quench tank is periodically purged into the system slag



pit.







     The volatile products of pyrolysis and products of



primary combustion exit from the gasifier into the secondary



combustion chamber, where the gases are mixed with a near-



stoichiometric quantity of ambient air.








     The secondary combustion chamber is a vertical, refractory-



lined vessel in which temperatures of 1,400 C  (2,500 F) are



realized and where sufficient residence time to assure



complete burning is maintained.  The majority of the particulate



matter entrained in the off gas from the gasifier is burned



or slagged-out into another slag-quench tank.  The resulting



slag residue is sluiced into the system slag pit.  The



combusted gaseous mixture exits from the secondary combustion



chamber at 1,150 to 1,250 C (2,100 to 2,300 F) .








     A portion of the hot waste gas from the secondary



combustion chamber (about 15 percent) is directed through



regenerative towers where its sensible heat is recovered and



used for preheating the process air supplied to the gasifier



hearth.  These regenerative-towers, successfully used for



many years in the steel industry, are two refractory-lined



vessels containing a high heat capacity refractory checkerwork



material.  Hot products of combustion from the secondary



combustion chamber and ambient process air are passed through
                               42

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                                                           512



the towers on a cyclical basis for preheating the 1,000 C



combustion air.  The remainder of the flow exiting the



secondary combustion chamber is supplied to a waste heat



boiler designed for inlet gas temperatures of 1,150 C to



1,250 C (2,100 to 2,300 F).








     The cooled waste gases from the regenerative towers are



combined with the exiting flow from the waste heat boiler



and are ducted to a hot gas electrostatic precipitator of



conventional design.








     Status.  The principles of the Torrax process were



originally proven on a 68-tonne  (75 ton)-per-day pilot plant



operated intermittently from 1871 to 1975.  This plant,



located in Erie County, New York, and financed with a grant



from EPA has been used to process municipal solid waste and



solid waste/ sewage sludge mixtures.  Tests with controlled



percentages of waste oil, tires, and PVC plastics were also



run.  The pilot plant differs significantly from the above-



described system in that the hot-blast combustion air is



heated using a gas-fired air-to-air heat exchanger instead



of the regenerative towers.








     The Carborundum Corporation, which was involved in the



original development of the Torrax process, has turned its



marketing rights over to Andco.
                              43

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                                                      513

     A 180-tonne (200 ton)-per-day prototype plant has been

built In Luxemburg and has been operating for over 1 year.

Three other Torrax plants have been built in Europe and are

in various stages of start-up.  They are located in Frankfurt,
                                              \
Germany; Grasse, France; and Centeuil, France.



                         Conclusions



     The first half of this decade has been characterized by

a flurry of activity related to energy recovery from municipal

solid waste.  Many communities acted hastily as a result of

intense environmental pressure.  This has led to the construction

of some facilities that are not working as efficiently as

was originally expected.  The lessons that have been learned

have/ in some cases, been very costly, both politically and

economically.



     With more plants coming into operation each year, a

great deal is being learned about the realities of what can

be expected from a solid waste energy recovery system.  And

while interest is every bit as intense as it had been in  the

past, community planners are moving more cautiously.  Resource

recovery is not the panacea,that will turn  "garbage into

gold," but it can be an economical means of waste disposal

if it is carefully developed.
                               44

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                                                                          514
           The Recovery of Energy from Municipal Solid Waste
             (A Review of Activity in the United States)
             Discussion Leader:   Mr.  David B.  Sussman
Question:  In the Harrisburg plant,  would you tell  me the type of

           shredder that is used and the reason why that shredder must

           be used to reduce the refuse to less than 5 cm in size,

           despite the fact that the shredder is not used in the Chicago plant?

Answer:    Some of the mass burning plants have installed shredders

           —hammermills—to reduce the bulky refuse to small sizes

           so that it can get into furnaces.  The reason for the

           shredder is to handle the bulky waste that comes to the

           facility; if no bulky waste comes to the facility, they

           would not need a shredder.

Question:  In the case of "small two chamber modular combustion units",

           is it possible to clear the air pollution limits for gas and

           dust emission with only the provision of afterburners?

Answer:    In this country, we only have a dust emission standard for

           incinerators—no gas standard.  And the  units can meet the

           present dust standard.  However, in the  future,  the dust

           standard will be tightened and the units will require

           additional air pollution control equipment to meet the

           new standards.

Question:  The paper mentions the use of catalysts  for pyrolysis systems.

           Is there any system using catalysts now underway in the U.S.?

           If there is, please let us know about it.

-------
                                                              515
Answer:    As the pyrolysis systems are experimental, various companies




           have tried different pressures and temperatures to make their




           systems produce specific pyrolysis products.  Two pyrolysis




           systems that I know of off hand use catalysts: one is a




           secret,proprietary catalyst; the other isaluminum  silicate,




           I think.  Neither system works.




Question:  It describes that pressure for various pyrolysis processes




           range 1 to 70 atmospheres.  What are the differences in the




           experimental results according to pressures?  What are the




           advantages for using higher pressure?



Answer:    I don't know what the advantages are because none are working




           at commercial scale.




Question:  How big was the pilot plant before going on to the 1000 t/d




           demonstration plant in Baltimore.  Couldn't it be possible




           to foresee the mechanical problems encountered in the 1000




           t/d at the pilot plant stage?



Answer:    The plant was scaled up from 35 t/d to 1000 t/d.   This was a




           mistake.  Yes, it was possible to foresee some of the mechani-




           cal and thermal problems because of this scale up;  but we all



           went ahead anyway.




Question:  The report  says that the San Diego project has been interrupted.




           What is the most recent status after the time of publication?




Answer:    The San Diego pyrolysis plant has been shut down.   The problems




           are with the production of the feed material and with the




           thermal process.   Occidental Research is studying the process

-------
                                                                      516
           to determine if it makes sense to continue investing money in




           the system.




Question:  In the St.  Louis plant,  as  an example  of refuse  derived fuel




           (RDF), I would like to  know the power  consumption in kilowatt




           hours per ton of refuse and the average  total  cost in dollars




           per ton of refuse for obtaining the  RDF  of less  than 1.5




           inches in size.




Answer:    The power consumption was 4O kilowatt  hours per  ton to pro-




           duce an RDF of approximately 1.5 inches  in size.  The cost




           to produce the RDF in St. Louis is not a good  number because




           the plant was pilot scale.   But the  cost of shredding  solid




           waste averages about $3.00 per ton.




Question:  In the Baltimore pyrolysis  plant,  would  you please explain




           more details concerning the problem of blockage  in the waste




           storage bin and feeder and  the failure of the  residue drag




           conveyer?



Answer:    It was a 1000 ton storage system.   The problem was with




           abrasive wear between the buckets that dragged the material




           out and the floor, and the  fact that stored garbage formed a




           dense mass and would not feed out.  The  failure  of the residue




           drag conveyer was caused by large pieces of slag jamming the




           conveyer; the slag was formed during process upsets.




Question:  What are economic evaluations for various types  of pyrolysis




           processes under development?




Answer:    So far, none of them are economically  viable.  You don't evaluate




           something that is not economically viable anyway.

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                                                                       517
Question:  Among the 'four main pyrolysis systems described in the paper,




           which process is considered the most promising?




Answer:    Two have failed; one works in Europe and the other one they




           can't seem to sell.  Therefore I would have to answer that




           I don't think pyrolysis of mixed municipal solid waste is




           very promising at all in this country within the next five




           to ten years.




Question:  You mentioned that of the four main pyrolysis projects, one




           works in Europe.




Answer:    That's right.  That's the Torrax System that was developed




           here in this country.




Question:  Why does it work there?




Answer:    Well, I don't consider it pyrolysis, number one.  I consider it




           starved air combustion.  It is just another form of burning




           garbage.  Whether it will be competitive in this country




           compared to other garbage mass burning techniques still



           remains to be seen.  The only true pyrolysis system that




           we have in this country is Union Carbide's  Purox.  And




           they haven't sold a commercial version yet.  Nobody wants to




           buy it.  It's too expensive.




Question:  I understand that this Purox system developed by Union Carbide




           is supposed to enter the Japanese market very soon.  We are




           told that the capacity will be 75 tons per day for each of




           the two units; so tha't makes 150 tons per day.  Would you




           like to make some remarks on this?

-------
                                                                       518
Answer:    Well, the Union Carbide system does work.   It has operated at




           150 tons per day for a 90 day period—steady.  When Union




           Carbide has attempted to sell that unit in this country it




           costs so much more than competing technologies that no one




           would buy it.  What I'm saying is that I have yet to see




           the commercial viability of the Union Carbide process in




           this country.  It may work fine in Japan because your waste




           is quite a bit different from ours and your problems are




           different.  I want to bring up one more point.  Five years




           ago, Kawasaki was promoting Monsanto's Landgard system in




           Kobe, Japan—30 tons per day.  When Baltimore did not work,




           Kawasaki stopped promoting Landgard.  I can only say that




           perhaps Union Carbide and the Japanese affiliate of Union




           Carbide have the same arrangement.  It hasn't sold here;




           maybe it will sell there.  One more point.  It is our opinion




           at EPA that there have been no successes with pyrolysis but




           as a developmental technology it still has promise.  It is




           just that it is not ready for implementation today in a city




           —maybe in five years; maybe ten years.



Question:  What are the advantages and disadvantages  of using a wet




           system for mass burning?




Answer:    I was avoiding answering that question because you are going




           to go to Hempstead and I'd rather the system developers give




           you their opinion of why it is better, rather than put me on




           the spot.  That's saying I don't want to get involved.  I

-------
                                                                              519
           can't really give you the advantages and disadvantages because




           I don't have the data to support an opinion.  I have never




           seen an energy balance sheet on the Hempstead plant.




Question:  As to the two chamber combustion systems, are there any cases




           with dust recovery?




Answer:    In the two-chamber unit, the primary chamber acts as a gasifier




           —a pyrolysis chamber.  It has very low air flow and very little




           dust is entrained in the gas stream.  In the second chamber,




           organic gases are combusted to completion.  Consequently,




           the whole system produces very little dust.




Question:  for what size population was the plant in Nashville designed?




Answer:    The plant operates on  about 500 tons of garbage a day.  That's




           only part of the population of the city.  It supplies




           steam and chilled water to a number of buildings in the downtown




           area	it's not the whole city.




Question:  Your report is very helpful and very informative.   And I am




           very glad to be here to listen to your report.   I don't mean




           to give you a hard time, but could we possibly have what



           you just explained to us in written down form,— in the form of




           documents or something?




Question:  On the whole technology?




Answer:    Just the answers you h>zve yiven us to these questions.




Response'  I can send you all kinds of documents as we get them in or




           I can formally answer your questions.  However there will be




           a written version of the question and answer segment of this




           conference.




Response:  The written version of the question and answer segment of this




           conference will be satisfactory.

-------
Comment:   I think what I should do is go to Japan and sit  down with you




           and we can go over this again. (Laughter)



Comment:   What Dr. Naito is concerned about is that  to many of us,  what




           you just told us is somewhat shocking.   So what  we are  con-




           cerned about is knowing if this statement  is available  in the




           future as an appendix to your report—in other words, as




           an official statement of EPA.




Comment:  Mr. Sussman's self-incriminating remarks will be  part of the




           transcript. (Laughter)




Question: One of the questions I was asked earlier was whether the Depart-




          ment of Energy shares this view of of this  technology.   Maybe




          Steve, you can reflect DOE's feelings on pyrolysis both  today




          and in the future.




Answer:   I would say that Mr. Sussman's comments represent the general




          American government viewpoint—both of DOE  and EPA concerning




          the status of pyrolysis.  I don't think there is  any conflict.

-------
                                                            521
5.1,   RESEARCH AND DEVELOPMENT OF RESOURCES RECOVERY SYSTEM

                       (SECOND PHASE)
        Ministry of International Trade and Industry
        Agency of Industrial Science and Technology

        1-3-1, Kasumigaseki, Chiyoda-ku, Tokyo

-------
                                                                  522
                         CONTENTS


                                                                 Page


1.   Introduction  	     1


2.   Purpose of Research and Development 	     1


3.   Research and Development of Material Recovery Type Process
     Sys tern	     2

     3.1  Assortment of Urban Wastes 	     4

     3.2  Converting Wastes into Compost 	     6

     3.3  From Was tes to Refined Pulp 	     7

     3.4  From Wastes to Fuel Gas 	     9


4.   Research and Development of Energy Recovery Type Process
     Sys tern	    11

     4.1  Pre-treatment of Urban Refuse 	    13

     4.2  From Garbage to Methane  	    13

     4.3  From Wastes to the Fuel Oil 	    13

-------
                                                                  523
1.   Introduction
     The Agency of Industrial Science and Technology,  Ministry of
     International Trade and Industry, carried out research and develop-
     ment of the elementary techniques of a system for utilizing urban
     solid wastes, in the period of fiscal 1973 to 1975 as a part of the
     big industrial technical research and development system planned by
     Japanese Government.  The secondary phase of research and development
     was started from fiscal 1975.   It aims at an integration of the
     previously developed elementary techniques into an innovational
     technique useful for recovery  and reuse of urban refuse (domestic
     wastes).  An experimental test plant, called the  "Star dust *80",
     is at the most advanced stage  in the above-mentioned "Research and
     Development of Resources Recovery System" project and is seen as
     the most promising urban refuse recovery and reuse process system in
     the 1980rs.
2.   Purpose of Research and Development
     The following is the fundamental purpose  of  the  secondary-phase
     research and development of this resources recovery  system:
     (1)  To realize synthetic and effective treatment necessary  for
          converting collected mixture of  urban solid wastes  into useful
          and harmless resources.
     (2)  To make it possible to convert a large  part of  recovered
          waste into material resources and energy  resources.
     (3)  To meet the requirements for preventing environmental pollution.
     (4)  To develop a system which is safe and relatively  easy to
          maintain.
     (5)  To develop a system which will be more  economical than  the
          currently  existing systems when  taking  the  subsidiary effect
          of utilized resources into consideration.
     (6)  To develop a system well fitted  to social needs.
                                 -  1  -

-------
                                                              524
The method of research and development is as follows:
Two prototype technical systems are set up:   One for mainly
reproducing material resources and the other for mainly recovering
energy resources.  For each system, a large-sized pilot plant
(treatment capacity is about 100 tons a day) will be designed and
constructed.  Through the long-term test operation of the pilot
plants, useful data will be obtained for establishment of necessary
techniques on design, construction and operation of an actual plant
which satisfies the above-mentioned purposes of development.
Research and Development of Material Recovery Type Process System
(Star dust '80)
This research and development effort concerns a technical system
which converts a considerably large part of urban solid wastes
mainly into material resources.   A pilot plant (100 tons a day in
capacity) under this system is under construction on reclaimed ground
in Kanazawa-ku, Yokohama City, Japan.  Figure 1 indicates the
schematic flow of this pilot plant.
The pilot plant consists of the following sub-systems:
(1)  A pre-treatment sub-system around the semi-wet selective
     pulverizing classifier which classifies the mixture of collected
     wastes into garbage group,  wastepaper group and plastic-and-
     metal scrap group.
(2)  The high-rate composting sub-system which converts refuse of
     the garbage group into compost (farmyard-manure-like, organic,
     soil improvement compound).
(3)  The pulp-refining sub-system which converts wastepaper into
     refined pulp.
(4)  The two-bed type pyrolysis sub-system which converts recovered
     plastics into fuel gas.
                            - 2 -

-------
                                                                                               525
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                                                                     526
3.1  Assortment of Urban Wastes   (Pre-treatment  sub-system)
     Figure 2 indicates  the  principle  of  the  semi-wet  selective  pulverizing
     classifier — the main  part  of  the pre-treatment  sub-system.   The
     device is composed  of the  rotary  drums,  which  have  two  kinds  of
     screens different in mesh  from  each  other,   and two kinds of  scrapers
     which correspond to the two  screens,  respectively,  and  rotate at
     different speeds from each other.  Charged  wastes are crushed as
     they are pushed in  the  axial direction of drums,  and assortment  of
     wastes can be attained  by screening  them out of the drums,  according
     to the different sizes  of  the crushed grain size  of materials due to
     the differences in  shock resistance,  compression  resistance and
     shearing stress properties.

     When a mixture of wastes is  thrown into  the classifier, the scrapers
     will first crush the most  fragile material  such as  garbage, soil and
     glass, and crushed  material  will  be  collected  through the first-stage
     screen (group I).  The  remaining wastes  are wetted  with water in the
     drum and subjected  to shocks, shearing and  crushing by  scrapers
     while they move in  the  drums.  Wetted wastepaper  will therefore  be
     collected through the second-stage screen  (group  II).   Metal-and-
     plastic scraps with the highest ductility will come out of  the
     opposite end of the drums  (group  III).   The features of this  pre-
     treatment sub-system are as  follows:
     (1)  Simultaneous crushing and  assortment  function  can  be achieved
          by a light-power,  single process.
     (2)  Group I material mainly composed of garbage  is favorable raw
          material for compost.
     (3)  Group II material  mainly composed of wastepaper is favorable
          raw material for  refined pulp.
     (4)  Group III material mainly  composed  of  plastics is  favorable
          raw material for  fuel gas.

-------
                                                        527
(5)  In accordance with variation in composition of  charged wastes
     assortment can easily be modified by adjusting  the speed of
     feeding vraste into the drums and the relative speed of rotation
     of scrapers to the drums.
(6)  Unlike the conventional overall crusher,  this device allows
     metal, rubber, leathers, clothes and plastics to remain nearly
     the same sizes as their original state, thus eliminating the
     problem of heavy metals contained in the  compost caused by
     crushing batteries and exfoliation printing ink.
(7)  The device is provided with a protector which prevents tangling
     of long strings and a safety device which prevents overloading.
An example of assortment of urban wastes is shown in Table 1.
          Table 1   Results of Experiment by Small
                    Continuous Experimental Model


Paper
Garbage
Glass
Soil, Sand,
Stone
Metals
Plastics
Fibers
Wood and Bomboo
Pieces
Total
Moisture
Content
Separation by Groups
(Dry Basis) %
I

43.5
88
88.5
74.5
19.5
11
8
24.5
51.5
-
II

42
11
11.5
23.5
2.5
7.5
15.5
27
24.5
-
Ill

14.5
1
0
0
78
81.5
76.5
48.5
24
-
Total

100
100
100
100
100
100
100
100
100
-
Composition by Groups
(Dry Basis) %
Before I
Charging
48.6
21.3
5.6
2.3
4.1
14.4
2.7
1.0
100
49
41.5
39.5
10
3.5
1.5
3
0.5
0.5
100
61
II

80
8.5
2
2
0.5
4.5
1.5
1
100
66
III

32
1
0
0
12
45
8
2
100
26
                            - 5 -

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                                                              528
3.2  Converting Wastes into Compost   (High-rate  Composting Sub-system)
     Garbage selectively collected by the  pre-treatment  sub-system is
     converted into good quality farmyard-manure-like  organic manure
     by the high-rate composting sub-system.

     Garbage contained in the fermentation vessel  is satisfactorily
     stirred up at fixed intervals of time and fed with  air,  so that
     vigorous fermentation activity  can convert  garbage  into  odorless
     manure in a short period.  Foreign matter such as glass  fragments
     and small pieces of plastic are removed.  The high-rate  composting
     sub-system not only contributes to producing  good quality organic
     manure, but also to saving space in land to be filled up with urban
     was tes.
     The features of the high-rate composting sub-system are  as follows:
     (1)  Mechanical stirringTIand forced aeration  in the functionally
          designed fermentation vessel accelerate  activity of micro-
          organisms so that garbage  can be converted into organic manure
          in a short period of time.
     (2)  Manure product is free from foreign matter,  uniform in grain
          size, and stable in quality.
     (3)  The machine is designed as an economical, automatic system.
          Its running cost is quite  small.
     (4)  Manure product is hygienic since the heat (70°C) generated
          during fermentation kills  disease germs  and  parasites and
          dissolves seeds which may  be in  garbage.
     (5)  Counternieasures are taken  to prevent generation of  bad smells
          and other environmental pollution which  frequently  accompanies
          conventional composting systems.
                                 - 6 -

-------
                                                                     529
     The manure product includes the  following fertilizer  components:

          Nitrogen (N)              1.6  to 2.3% (weight proportion)
          Phosphate (P20s)          0.8  to 1.2%
          Potassium (K£0)           0.7  to 3.1%
                        First stage Second stage
                Charged wastes   I screens  I Scrapers
                            Group  I   Group  IX  Group III
                     Fig-  2   Principle  of  Semi-wet  Selective
3.3  From Wastes to Refined Pulp   (Pulp-refining sub-system)
     This sub-system is for removing plastics, waste  threads, hairs  and
     garbage from the wastepaper  which  is  selectively collected by the
     pre-treatment sub-system,  and for  producing sterilized, bleached and
     refined pulp.  Refined pulp  can be used not only for paper manufacture,
     but also for other applications which require  supply of new pulp.
                                 -  7  -

-------
                                                         530
The results of experiment made in laboratory on the quality and
other characteristics of the pulp collected  from urban solid wastes
by the semi-wet selective separator are as  described in the following.

(1)  Quality
     (a)  Compared with the pulp regenerated from used waste paper,
          the pulp under consideration contains a slightly greater
          amounc of inclusions such as wool  and thread pieces, straw
          pieces, wood fragments, hairs and  plastics (including hot-
          ffielt basic adhesives) .
     (b)  The burst factor, breaking length  and tear factor of the
          pulp under consideration are between those of used newspaper
          regenerated pulp and those of used cardboard regenerated
          pulp.

(2)  Deinking             ;,
     (a)  The tested urban solid wastes contained paper by an
          average of 35.0 percent.  The paper consisted of newspaper
          and magazines 55.7%, cardboard 26.7%, kraft paper 9.8%
          and high quality paper 7.8%.
     (b)  Under the condition staged above,  the percentage of
          additives such as alkaline chemicals and surface active
          agents and the processing temperature had little effect
          upon the deinking.
     (c)  The pulp under consideration assumes the color of kraft
          paper, without remarkable improvement for whiteness by
          the deinking.

(3)  Sanitary Factors
     o  Stink
        (a)  The as-separated paper from urban solid wastes (Group
             II) evidently stinks of kitchen refuses.
                            - 8 -

-------
                                                                  531
             (b)   As the separated paper Is pulpified,  this  stink  is
                  removed and the pump  has  the smell of old  waste  paper.
                  The sterilizing treatment in the pulpifying process  has
                  an effective influence upon the removal of the stink.

          o  Colon Bacilli
             (a)   The number of colon bacilli is counted as  the index  of
                  bacterial contamination.
             (b)   In this test, the number  of colon bacilli  in the separated
                  paper was 108 to 10^  but  was reduced  to less than 10^ in
                  the processed pulp.

          o  Other Harmful Inclusions
             The  concentration of alkyl mercury (R-Hg), total mercury  (T-Hg)
             cadmium (Cd), lead (Pb), total chromium (T-Cr), arsenic (As),
             cyanides (-CN), organic phosphorus (R-P) and polychlorobiphenyl
             (PCB) has been measured to indicate no significant amount of
             them present in the pulp.
3.4  From Wastes to Fuel Gas (Two-bed type pyrolysis  sub-system)
     This sub-system is for effectively converting the plastics  selectively
     collected by the pre-treatment sub-system into good-quality,  high-
     caloric (7,000 Kcal/m^) fuel gas.  The two-bed type  pyrolysis sub-
     system is so called because it uses circulation  of fluidized  medium
     (sand) between two beds so that pyrolizing  reaction (endothermic)
     and combustion reaction (exothermic)  can be performed independently.
     The features of this pyrolysis system are as follows:
     (1)  Fluidized sand is heated by combustion of char  formed  by the
          preceding thermal decomposition  in the pyrolizing reaction.
          The fluidized sand is then circulated to the regenerator and
          gives its heat to waste to cause gasification of the waste by
                                 -  9  -

-------
                                                                532
     thermal decomposition.  Char, residum of thermal decomposition,
     is sent to the primary bed.  Gasification of waste is supported
     by repetition of this process.
(2)  Since char is used for heat source, thermal decomposition is
     attended by formation of a little quantity of solid solution
     and tar-like material which are difficult to deal with.
(3)  Since the regenerator and the pyrolizing reaction are separated
     from each other, gas product can be used for fluidized gas which
     is to be circulated inside the pyrolizing reaction, thus making
     it possible to produce high-caloric gas.
(4)  Piping which connects the two beds to each other is specially
     designed so as to give the fluid bed turning movement.   Other
     unique designs are applied to the feeder of waste, etc.
For details, see the separate volume "Two-bed Type Pyrolysis  (from
Wastes to Fuel Gas)".
                           - 10 -

-------
                                                                533
4.   Research and Development of Energy Recovery Type Process System

     This research and development effort concerns a technical system
     which converts some part of the mixture of urban refuse mainly into
     energy resources (fuel oil and methane).

     Figure 3 indicates an example of composition of urban refuse in
     Japan.
             Water content
                49.0%
                                    Combustibles
                                              36.4%
Wastepaper
  21.4%
                                 Low
                             • calorific     ,^_-—Plastics  5.1%
                              value      "(Tncl. vinyl chloride)
                             1458 Kcal/kg	—-_____08%)
                                              Garbage
                                                      4.2%
                                                                  Wood and
                                                                  miscellaneous
                                                                  material
                                                              Waste threads
                                       grave
                                    3.33.6%
                                            Non-
                                   combustibles
                                •Metal scrap

                'Eggshell and shells  0.5%


            Fig. 3   Example of Composition of Urban Refuse

                                -  11 -

-------
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                                                                      535
A.I  Pre-treatment of Urban Refuse
     The pre-treatment of urban refuse includes the opening of bags filled
     with nixture of wastes, the primary crushing of the mixture,  and the
     separation of garbage from other organic wastes (plastics, wastepaper,
     etc.) using a machine.  Garbage is put into the wet-type separator
     machine which separates the raw material for the methane-fermentation
     process from useless material.  The other organic wastes are  subjected
     to secondary crushing, dried by waste heat from the fluidized thermal
     decomposition process, and used for raw material of thermal decomposi-
     tion.

4.2  From Garbage to Methane (Methane fermentation sub-system)
     This sub-system employs a new methane fermentation technique  (two-bed
     type) which makes it possible to convert garbage into methane in a
     short period of time.  In this system, garbage slurry is first liquefied
     in the first bed (liquefaction bed).   Liquefied material is then
     subjected to methane-fermentation process in the secondary bed (gasifi-
     cation bed).  Effective production of finest methane can thus be
     obtained.

4.3  From Wastes to the Fuel Oil (Fluidized Thermal Decomposition  Sub-
     systeu)
     This sub-system is for mainly converting selectively collected plastics
     and wastepaper into fuel oil by means of fluidized thermal decomposition
     method.  Waste heat of steam and off-gas accompanying thermal
     decomposition is utilized for heating the fermentation bed of the
     methane fermentation sub-system and drying raw material.

     For details, refer to the separate volume "Fluidized Bed Pyrolysis"
     (from Wastes to Fuel Oil).
                                - 13 -

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                                                         536
Basic study of every sub-system is almost  completed.   Basic design of
a pilot plant (treatment capacity:  100 tons  a day) has  been completed,
too.  We are now ready to start manufacturing design  and construction
of the pilot plant.
                           - 14 -

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                                                                    537
                 R and D of Resource Recovery Systems
            Discussion Leader:  Mr.  Hideaki Takamatsu
Question:  How much is the current funding commitment in terms of

           dollars for these systems?

Answer:    It is 100% funded by the government.  If we examine the plant

           in Yokohama City, construction  costs of that facility amount

           to 300 million yen or approximately 32 million dollars.

Question:  What is the next step after the 100 t/d units are successfully

           tested.  Are "demonstration tests" planned at 1000 or 2000 t/d?

Answer:    Before I directly answer the question I would like to mention

           that one component classifier can handle 100 t/d per 8-hour

           operation.  In other words, if we operated the plant classifier

           around the clock, we would handle 300 tons.  We are continuously

           comparing the results of this plant with other incinerators.

           The average figure for incinerators of large municipalities in

           Japan amount to about 300 t/d   Therefore we think that this

           is viable in comparison to existing facilities.  So we can

           handle 100 t/d by running three or four of these plants.

           As a final design, we are developing drawings for plants

           with 100 t/d capacities.

Question:  Will much economic data be generated on the pilot plants and

           will this data be available to the United States EPA for

           comment?

Answer:    Yes, we are expecting some economic data related to the operation

           of the plant.  With regard to the latter part of the question,

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                                                                    538
           which is,  will data be available to the EPA for comment, yes,




           we can satisfy your request when the time comes.




Question:  We are very interested in the "semi-wet pulverizer"—is




           this a very slow-rotating speed as opposed to our fast-turning




           hammermills that run at 1200 RPM or so?




Answer:    It runs between 15 and 30 RPM.   You can see the movement of




           dust.  I'd like to also comment that there has been minimal




           noise and vibration so far.  We can carry on a conversation




           in a normal way.




Question:  What is Japan's major interest or reason for promoting such




           system  (a) mostly as an environmental protection measure;




           (b) primarily to conserve fibers, metals, etc.; or (c)




           just as a disposal method?




Answer:    Our original purpose would be: (b) primarily to conserve




           fibers, metals, etc.  But our intention would be: (a) most-



           ly as an environmental, protection measure.

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                                                539
       5.2   TWO-BED TYPE PYROLYSIS

            (FROM WASTES TO FUEL GAS)
Ministry of International Trade and Industry
Agency of Industrial Science and Technology
1-3-1, Kasumigaseki, Chiyoda-ku, Tokyo

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                                                                     540
                          CONTENTS







                                                                   Page








1.   General Description 	    1






2.   Gas Components  	    3






3.   Treatment of Pyrolysis Waste Water 	    7






4.   Heavy Metals and Carbon in Pyrolysis Ash 	   10






5.   Elimination of Aluminum Mixed in Urban Waste 	    11

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                                                                    541
1.  General Description
    The two-bed type pyrolysis system, which uses fluid!zed thermal
    decomposition process, is for gasification of plastics selectively
    collected by the pre-treatment sub-system of urban wastes.   Various
    types of pyrolysis systems have been tested for thermal decomposition
    of urban refuse.  This two-bed type system allows fluidized medium to
    circulate between the two beds (reactors); the primary bed is for
    endothermic reaction, thermal decomposition and gasification of waste
    and the secondary bed is for exothermic reaction, combustion of carbon
    residuum (char) attending gasification of waste.  It is a characteristic
    feature of this system to produce high-caloric fuel gas from urban
    wastes by separating thermal decomposition and combustion from each
    other.  Although the two-bed type pyrolysis has many actual results in
    the field of petrochemicals industry, application of it to treatment
    of urban waste requires special consideration.  Design of the appliance
    must include new ideas to deal with poisonous, corrosive gas which may
    be included in the gas produced from urban wastes, since raw material
    selectively collected from urban wastes is a hetrogeneous solid
    material and includes various kinds of foreign matter such as inorganic
    substances.

    Figure 1 indicates the schematic flow of two-bed pyrolysis plant.

    This plant consists of the pyrolysis reactor through which fluidized
    medium circulates, the regenerator, the precombustion burner, the raw
    material feeder, the cyclones, the heat exchangers, the vapor-liquid
    separator, the gas recycle blower, the air feeder, the gas exhaust
    blower, the gas cleaner and the produced-gas combustion device.  The
    plant also includes various auxiliary equipment, the devices for
    measuring and recording flow rate, pressure and temperature, as well
    as the automatic analysis for gas.
                                 - 1 -

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                                                             542
              Aluminum eliminator
                            Regenerator
        Cyclone
Heat exchanger
  Exhaus t gas
    Metal and noncombustibles
    Heat  exchanger
     Gas cleaner
      Produced pyrolysis gas
Recycle blower
-Pre-feeder
      Fig.  1    Schematic Flow of Two-bed Pyrolysis

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                                                                543
    Regarding design of this apparatus,  the pyrolysis  gas  product circulation
    system is adopted to provide increased thermal efficiency,  easy vapor-
    liquid separation and increased calorific value of gas product.   The
    pipe which connects the two beds to  each other is  not  provided with
    any moving valve; rate of circulation  of fluidized sand is  controlled
    by adjusting flow rate of a very small quantity of air flowing in the
    vertical conveyance portion.  To bring air pressure inside  the beds
    close to atmospheric pressure, the char and grain  catching  device of
    dual exhaust valve type is designed  with special care  against possible
    pressure loss.   The same consideration is paid also to design of the
    heat exchangers and vapor-liquid separator so that pressure loss by
    them can be minimized.  In the raw material feed,  the  gas sealing
    property of which is largely affected  by the level of  material in the
    hopper, the solid material overflow  system is adopted  so as to maintain
    the proper level of raw material, and  the gas sealing  portion is separated
    from the fluidized bed.  All conveyers which handle fluidized sand and
    raw material are fully enclosed to prevent sand and raw material from
    scattering.   Operation of the plant  is automatically controlled at the
    centeral control room.  Because this is a gas producing facility, it
    is equipped with an abnormality watching device, alarm device and
    emergency stop  device.
2.   Gas Components
    Tables 1 and 2 indicate the  produced  pyrolysis  gas  components  and
    the constituents  of exhaust  gas,  respectively,  obtained  as  the result
    of two-bed type pyrolysis  test.   The  figures  2  and  3  indicate  the
    correlation of gas  yield vs.  temperature  and  the  distribution  of
    carbon, respectively.   Table 3 shows  the  heavy  metal  contents  in  non-
    combustibles and  ash.

    When using the group III separated by the semi-wet  type  pre-treatment
    apparatus, the produced gas  is mainly composed  of methane,  carbon
    monoxide and hydrogen and  its calorific value is  as high as 7,000 Kcal/m3,
                                 -  3  -

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                                                              544
Yield of gas produced is 0.5 to 0.6 m^ per 1 kg of raw wastes.
This will be attended with generation of hazardous gases in the pyrolysis
reactor, which are 2,000 to 4,000 ppm of hydrogen sulfide, 200 to 400
ppm of hydrogen cyanide, 10 to 60 ppm of sulfur oxide and 600 to 2,000
ppm of hydrogen chloride.  Constituents of these hazardous gases can
be reduced within the regulated values by alkali cleaning and water
cleaning before collecting the produced gas.  In the regenerator,
scarcely any hazardous gases are generated because of combustion of
only char produced in the pyrolysis reactor.  A compact gas treatment
equipment is effective enough to deal with such a small quantity of
hazardous gases generated in the two-bed type pyrolysis plant.
Generation of nitrogen oxide is negligible because this is essentially
a reducing atmosphere system.
               Table 1   Produced Pyrolysis Gas
                         Gas Components
~^--~-^^_^ Material
Component ^~"~~~-~-— -^__^
H2 %
02
N2
CO
C02 .
CH4
C2H4
C2H&
C3Hra
C4Hn
Kcal/Nm3
Calorific
value (net)
Total refuse
I + II + III
30.0
0.9
2.5
34.7
11.2
12.7
5.4
1.1
1.0
0.5
4,100
Classified refuse
II + III
20.2
0.9
2.1
26.8
16.9
16.7
6.7
3.6
4.5
1.6
5,670
Classified refuse
III
15.8
0.1
4.8
21.1
11.2
23.8
11.7
4.7
5.8
1.0
7,000
                             - 4 -

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                                                          545
Table 2   Constituents of Exhaust Gas (ppm)
"^---^^^ Material
Component ^^^^
HCL
NH3
HCN
S02
NO
N02
C12
Classified refuse
1.2 - 6
1.0 - 15
0.1 - 0.6
2.3 - 2.8
10 - 80
A - 20
0.5 - 0.9
Regurated value
430
(50)
(10)
K = 1.17
"\ NOx as standard
V (100)
(1)
Numerical values in the brackets are regulatory
standards for general exhaust gas.
                    - 5 -

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                                                              546
                Table 2   Test Conditions
Item
Supply of waste
Supply of air
Circulating gas
Supply of sand
Decomposition temperature
Measurement
65 kg/h
50 Nm2/h
0 Nm2/h
40 kg/h
500°C
The products resulting from pyrolysis of waste are oil, gas,
carbide (char and dust) and water.

Figure 2 indicates yield distribution of products in percentage

to the quantity of raw material.
                Gas
                30%
                                  Water 37%
                                  Char  8%
                                  Dust  5%
                                  Oil  17%
                                  P-oil  12%
                                 'C-oil   5%
                                     Noncombustibles 3%
                    Raw material 100•>
         Fig. 2   Yield Distribution of Products
                  (Relative to raw material)
                           -  6 -

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          Table 3   Heavy  Metals  In Noncombustib]es  and  Ash
                                (Elution Test)
                                                                           547
^~~-\^ Material
Component ^~\^^
Pb
Cd
Hg
As
Cr
Classified refuse
Noncom-
bustibJe
< 0.05
< 0.005
< 0.0005
< 0.05
< 0.05
Ash
< 0.0')
< 0.005
< 0.0003
< 0.05
< 0.05
Regulated
value for
landf illiug
< 3
< 0.3
< 0.005
< 1.5
< 1.5*
Regulated
value for
seaf illing
< 1
< 0.1
< 0.005
< 0.5
< 0.5*
                   Unit:  ppm
                   *:     In case of C
3.   Treatment of Pyrolysis  Waste  Water
    There is remarkable difference  between  waste  water  coming  from the
    pyrolysis line and that coming  from the combustion  line.   Waste water
    from the pyrolysis line is  a  mixture of  water resulting from pyrolysis,
    water content in raw material and  oil content in  raw  material.   Oil,
    about 10 percent of weight  component of waste water,  is separated from
    water and is either returned  to the pyrolysis reactor or utilized as
    fuel oil for the regenerator  to heat f.Uu'dized sand.   As waste water
    is of strong acidity, neutralization is necessary and the  facility
    must be made of acid-proof  material.

    Figure 4 shows waste water  flow in a pilot plant.   Water from the
    pyrolysis reactor includes  floating oil, which is first separated from
                                 -  1  -

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                                                                 548
the water with the floating oil separator.   Then,  solid substances
such as char and sand are separated from waste water with the mist
separator so that about 80 percent of water content  can be obtained.
Oil separated from waste water is sent to the  oil  reservoir and,  after
its purity is increased, sent to the regenerator to  burn together with
char.  Meanwhile, waste water free from oil and solid substances  is
reserved in the pit.  The water is sent to  the stripper where water  is
brought into contact with steam so reducing material can be vaporized.
Vaporized material is sent to the condenser which  separates vapor and
liquid from each other.  The resulting volatile matter is burnt in  the
regenerator in the same manner as mentioned before for combustion of
oil.  Water passed through the stripper is  adjusted  to about 10 pH
value and treated with cationic polymer flocculant and ferric chloride
to settle heavy metals.  The water, from which heavy metal sediment
is removed, is then sent to the oxidation tank, in which soda hypochlorite
is added to resolve cyanide by oxidation treatment.   Solid substances
resulting from these resolvent treatments are  settled down with polymer
flocculant and removed from waste water. Finally, waste water is
neutralized and drained through the sand filter and  the active carbon
absorbing tower to a sewer.  Figure 4 shows an example of the result of
water analysis before and after waste water treatment.
                             - 8 -

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                                                        549
Combustion:      J^
equipment1
        Mist
     separator1-
 Regenerator
                                         Spray tower
                                                  Water
  Active carfon
adsorbing towerm
              Sladge
                                  Separating water
                                  •tank1
    Fig.  4 Practical Pilot Plant Flow Sheet
                     - 9 -

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                                                                     550
             Table 4   Raw and Treated  Water Quality  of
                       Total Pulverizing Pyrolysis
                       Waste Water
Component
Cd
CN
T-P
Pb
T-Cr
As
T-Hg
PCB
pH
N-Hex
Phenol
Cu
Zn
Mn
BOD
COD
SS
Raw water
0.01 mg/1
85
< 0.1
0.1
< 0.05
< 0.05
< 0.0005
0.008
6.8
291
57
< 0.1
0.04
0.3
990
1520
-
Treated water
Trace
0.7
Trace
Trace
Trace
Trace
Trace
Trace
7.2
0.7
Trace
Trace
Trace
Trace
120
13
1
4.  Heavy Metals and Carbon in Pyrolysis  Ash
    The ash caught by the cyclone in the  combustion line is composed
    of ash content in raw material and pulverized fluidized sand.
    The ash, quantity of which is as small as about 20 g per 1 kg of
    raw material, includes high density of heavy metals.   Ash is fused
    together with glass, selectively collected from group 1, to make
    harmless solid matter which may be recovered as light-weight
    aggregates.   A result of tracing heavy metals in pyrolysis material
    shows that copper, lead and chrome remain mainly in fluidized sand,
    while mercury and cadmium remain in waste water.
                                 -10-

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                                                                      551
    As to material balance  based  on  carbon,  carbon  content  in  raw material
    is distributed by pyrolysis process  into gas, tar  and waste water  as
    shown in figure 3.  Less  than 60%  of total  quantity  of  carbon is
    included in pyrolysis  gas while  about 30% of  total quantity is  included
    in char and exhausted  from the regenerator  as off-gas.   The remainder
    forms tar,  etc.
5.  Elimination of Aluminum Mixed in Urban Waste
    After a long period of operation of the pilot  plant,  some  adhesive was
    found on the inner wall of the No.l cyclone  for  the regenerator,  it
    being feared that further progress of adhesion may cause possible
    lowering of dust-collection performance of the cyclone.  Thirty percent
    or more of this adhesive was aluminum.  It was assumed that the
    adhesive was caused by fragments of aluminum foil (such  as "cooking
    foil") mixed in raw material, which would be  carried into  the regenerator
    together with fluidized sand.  A part of melted  aluminum would be
    oxydized and carried into the flue to form resolidified  adhesives.   A
    protective method has been successfully achieved by the  use of an
    aluminum eliminator composed of a rotary body  placed close to the No.l
    cyclone and a scraper located on the back of  rotary body.   The rotary
    body forces aluminum to adhere to its surface.  Meanwhile, the scraper
    sweeps out adhesive from the rotary body.  Table 5 indicates the
    components of material collected by the aluminum eliminator.
         Table 5   Components of the Powdery Material Captured
                   by the Aluminum Eliminator
Component
%
Al
32
Fe
0.24
Zn
0.46
Mg
0.04
A1203
15
Si02
19
Fe203
4.2
C
1.5
H20
5.6
                                - 11 -

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                                                                    552
                        Two-Bed Type Pyrolysis
                  Discussion Leader:  Mr. Hideaki Takamatsu
Question:  Has the unit operated on unsorted waste?

Answer:    This system is primarily designed to have plastic removed

           from mixed waste.  This system cannot handle unsorted waste.

Question:  How is the waste separated?

Answer:    As I mentioned, a pulverising classifier separates the waste.

Question:  What is the diameter of the Two-Bed Type Pyrolysis?

Answer:    460 millimeters.  I would like to mention some of the trials

           we made before we set this up.  We tried 300 millimeters in

           diameter; 100 millimeters and finally 460 millimeters.

Question:  One of the by-products in the process is a liquid material.

           Is that recoverable as a product and if not, how is the

           residue handled?

Answer:    There has not been a liquid by-product.  We burn the tar.

           Dr. Hirayama is a technical expert and he just answered

           this question by explaining that the tar recovered from

           this process takes two paths: one is recirculated to the

           thermal cracking system and the other goes into the burning

           process.

Question:  What is derived from the cracking process?

Answer:    The end product of the thermal cracking process is gasifi~

           cation.

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                                                     553
     5.3   FLUIDIZED BED PYROLYSIS

           (FROM WASTES TO FUEL OIL)
Ministry of International Trade and Industry
Agency of Industrial Science and Technology
1-3-1, Kasumigaseki, Chiyuda-ku, Tokyo

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                                                                      554
                          CONTENTS
                                                                  Page
1.   Introduction 	      1
2.   Basic Flow of Fluidized Bed Pyrolysis  Sub-system 	      1
     2.1  Pyrolysis Section 	      3
     2.2  Oil Recovery Section 	      4
     2.3  Heat Recovery Section 	      4
3.   Yield of Products and Thermal Balance  	      5
     3.1  Yield of Products 	      5
     3.2  Heat Recovery Rate 	      9
4.   Characteristics and Uses of Products      	     10
     4.1  Produced Oil	     10
     4.2  Char and Dust 	     12
     4.3  Gas 	     13
     4.4  Waste Water 	     13
5.   Actions of Harmful Components 	     13
     5.1  Noxious Gases 	     13
     5.2  Heavy Metals 	     14
6.   Effective Use of Resources Produced 	     17
     6.1  Combustion Test of Produced Oil	     17
     6.2  Combustion Test of Char 	     17
7.   Ease of Operation and Control of Pyrolysis Reactor 	     18
8.   Conclusion 	     22

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                                                                        555
1.  Introduction
    The fluidized bed pyrolysis system is an apparatus for recovering urban
    refuse by converting wastepaper and plastics into fuel oil through a
    thermal decomposition process.  This single fluid bed type pyrolysis
    reactor uses partial oxidization method for thermal decomposition of
    urban waste and has the following features:

    (1)  It is possible to recover mainly fuel oil which is more favorable
         for storage and transportation than other pyrolysis products.
    (2)  Because it is a single bed type, the apparatus is simple in
         structure and easy to operate.
    (3)  Fluidized thermal medium (river sand) in the pyrolysis reactor
         makes temperature in the reactor uniform and permits quick
         thermal conductivity to raw material (waste).  This assures
         treatment of a large quantity of dust per unit volume, with
         minimum time required for thermal decomposition of dust.  Also,
         it is possible to make the apparatus compact.
    (4)  Because the reactor does not require any mechanical driving
         mechanism inside the reactor, increase in high-caloric synthetic
         plastics content does not affect normal treatment of waste.
    (5)  Pyrolysis process is attended with generation of gas and char.
         The char can be used for solid fuel to assist combustion of muddy
         material.  While gas can be utilized for drying raw material and
         generating steam.
2.  Basic Flow of Fluidized Bed Pyrolysis  Sub-system
    Basic flow of this sub-system is shown in figure 1.
                                 - 1 -

-------
                                                                    556
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                  -  2  -

-------
                                                                  557
    The apparatus consists  of the pyrolysis  section which  is  the  main
    part of this process,  the oil recovery section, the heat  recovery
    section, the exhaust gas  treatment  system,  the utility section,  etc.
    Urban solid wastes are  subjected to previous  crushing  and assortment
    by the pre-treatment sub-system.  Raw material to be supplied to the
    pyrolysis reactor is organic such as wastepaper and plastics, which
    has been collected from urban solid wastes  separated from noncombustibles
    (inorganic matter) and  garbage,  and is smashed to 50 mm or smaller
    pieces.  The contents  of  wastepaper, plastics and water included in
    the raw material largely  affect  the recovery  rate of oil.   Therefore,
    raw material is dried  until 30%  or  less  water content  by  the  drying
    process before it is brought into the pyrolysis reactor.   It  is
    desirable to minimize water content of raw  material, because  much
    moisture causes heat loss in the pyrolysis  reactor due to latent heat
    of evaporation, increase  in raw  material consumption using to compensate
    for heat loss.  For heat  source  of  drying process, gas generated from
    the pyrolysis reactor  is  burnt in the heat  recuperator so that sensible
    heat of exhaust gas of  the furnace  is utilized to heat air.   The
    following is an outline of each  section  of  the fluidized  bed  pyrolysis
    sub-system.
2.1  Pyrolysis Section
            »
    The fluidized bed pyrolysis  reactor is  adopted.   This  partial  oxydizing
    pyrolysis  method is  used for causing decomposition  reaction  under
    insufficient air supply, and product is affected  not only by composition
    of raw material, but also by reaction time,  temperature  and  pressure
    as well as by existence of catalyst.  The energy  recovery system is
    to compensate for large energy loss accompanying  the conventional
    incineration and aims at recovery  of stockable oil.  From viewpoint of
    oil recovery, it is  desirable to lower  reaction temperature  as far
    as possible.   On the other hand, a relatively high  temperature should
    be maintained to keep necessary reaction rate.  It  was found that
    about 500°C is high  enough temperature  to satisfy both of these
                                -  3 -

-------
                                                                  558
     requirements.   The  fluidized bed pyrolysis system  is single  in
     structure,  easy to  operate  and  most economical.  The superiority
     in maneuverability  of the 500 mm dia.  reactor over others was proved
     through over 1500 hours  of  test runs including 200 hours  continuous
     operation.
2.2  Oil Recovery Section
     Among the pyrolysis  products,  oil,  gas  and water  are  drained from
     the top of pyrolysis reactor.   The  gas  produced is sent  to  the  oil
     recovery section through the single-cyclone  and multi-cyclone dust
     collectors.   In the  oil recovery section, about 500°C of produced
     gas is cooled by the dual-stage scrubbers so that "plastic  oil"
     (P-oil produced by thermal decomposition of  plastics)  and "cellulosic
     oil" (C-oil produced by thermal decomposition of  cellulosic material
     such as wood and paper) can be obtained.  C-oil is mainly collected
     at the primary scrubber, outlet temperature  of which  is  maintained
     at 80"C; while P-oil is mainly collected at  the secondary scrubber,
     outlet temperature of which is maintained at 55°C.  C-oil and P-oil
     passed through the scrubbers are caught by the mist separator next
     to the secondary scrubber and  returned  to the secondary  scrubber.
     C-oil and P-oil collected by scrubbers  are separately stored in the
     respective reservoirs.
2.3  Heat Recovery Section
     Gas coming out of the mist separator in  the  oil  recovery section  is
     directed to the heat recuperator,  where  the  gas  is burnt with the
     help of burning of a part of recovery oil  since  calorific value of
     the gas is as low as 700 to 950 Kcal/Nm^.  Sensitive  heat of exhaust
     gas from the heat recuperator is recovered.   The heat recuperator
     is also effective to eliminate bad smells  because air from the raw
     material stock pit is used for supporting  combustion  of gas in the

-------
                                                                    559
     heat recuperator.   About 800°C of exhaust  gas  at  the heat  recuperator
     outlet is first directed to the air heater to  heat  air  for drying
     dust and then to the waste  heat boiler  to  produce steam to be
     consumed in this system.  Exhaust gas that lost its heat is then
     directed into the cleaning  tower to eliminate  HC1 and SOx.   The gas
     is finally emitted from the chimney.
3.    Yield of Products and Thermal Balance
3.1  Yield of Products
     An example of the result  of  experiment  using  the 500 mm  dia.  pyrolysis
     reactor is as follows:

     Table 1 shows the composition of  raw material used  in  this  experiment.
     Table 2 shows the conditions of pyrolysis  test.
           Table 1   Composition  of Raw  Material  (Average)
Item
Composition
(Z by
weight)
Wastepaper
Wood
Plastics
Non comb us tib les
Water content
Others
Bulk density
Crushed diameter
Net calorific value
Fixed carbon
Result of analysis
58.8
1.5
17.5
3.0
17.0
2.2
0.97 kg/1
30 - 50 mm
3,500 Kcal/kg
23 Wt %
                               - 5 -

-------
                                                                   560
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                            Temperature
                 Fig. 2  Gas  Yield vs. Temperature
                       Pyrolysis gas


                           58.13%
           Hazardous  gas
                                         f    Combustion

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                                                       Ash 1.07%
                                                       Drain 0.010%
                                 (Group-m)


                    Fig. 3   Distribution of Carbon
                                  - 6 -

-------
                                                           561
The yield of oils which was an object of the  test was  12% by weight
for P-oil, 5% by weight for C-oil,  and 17%  as a whole.  Water
produced by pyrolysis was 20% by weight, which was  the result  of
subtraction of 17% (original water  content)  from  37% of water
yield.

The yield of P-oil depends largely  on plastic and water contents
in the raw material.  Figure 3 shows  the property of waste which
affects yield of P-oil.
                           - 7 -

-------
                                                                                                                           562
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                                                            -  8 -

-------
                                                                     563
     It was found that  30  to 50%  of  plastics  originally included
     waste were converted  into P-oil.   The  yield  of P-oil  increased
     when water content decreased.
3.2  Heat Recovery Rate
     Figure 4 shows potential heat of products  in  percentage  to  the
     potential heat of raw material.
                      Gas
                      24%
                                      Char  14%
                                      Dust   4%
                                      P-oil 26%
                                      C-oil  6%
                                      Heat loss 26%
                        Raw material  100
                  Fig.  4   Potential Heat of Products
     The largest part of this heat-balance example was held by oil;
     P-oil 26%, C-oil 6% and total 32%.  This value is meaningful for
     recovering resources in the form of oil.  Percentage of other
     products was 24% for gas and 14% for char.  The remaining 24% was
     of heat loss, which includes both the sensitive heat from products
     and the heat loss from the apparatus.  Heat loss from the apparatus
     was approximately 12%, which is half as much as heat loss.
                                — 9 **

-------
                                                                  564
4    Characteristics and Uses of Products
4.1  Produced Oil
     Two kinds of oils,  called "P-oil"  and "C-oil",  are  produced by
     pyrolysis of urban  wastes.   Table  3 indicates  the result of
     characteristic analysis of P-oil.

                 Table 3   Characteristics of Plastic Oil
Item of analysis
Water content (% by
weight)
High calorific value
(Real /kg)
Low calorific value
Viscosity (cp)
C/H (-)
Average molecular weight
C
Elementary H
analysis n
(% by °
weight) S
N
Cl
Plastic oil
9.73
8,770
7,300
20 (65 °C)
6.87

70.87
10.31
8.09
0.10
0.46
0.27
Heavy oil *( reference
purpose only)
0.0
10,000
9,200
6 (15°C)
6.53

86.2
13.2
1.5
0.23
0.17
             *  Analysis is made in the same manner as that for
                plastic oil.
     Water content of P-oil was as much as 10% by weight when it was
     recovered by the scrubber in the form of emulsion.  The high
     calorific value of oil including 10% water content by weight was
     about 8,800 Kcal/kg and the low calorific value was about 7,300
     Kcal/kg.  Tnese calorific values are about the same as 10,000
                               - 10 -

-------
                                                            565
Kcal/kg of heavy oil.  Viscosity of P-oil was as high as 10,000 to
20,000 c.p. at ordinary temperature.  However, it lowered to about
20 c.p. at 65°C, allowing an atomizer burner to burn the oil.   The
C/H ratio was 6.87 which is approximately the same as that of
petroleum oils.

The average molecular weight was approximately 350.  Poisonous
elements were S (0.1% by weight), N (0.0% by weight) and Cl (0.27%
by weight).  Heavy metals were Cd (20 ppm), total Cr (10 ppm)  and
Pb (10 ppin) .  No Hg and As were detected.  When using P-oil as
fuel oil, it was feared that poisonous gases such as S02, NOx and
HCl might generate and heavy metals might volatilize.  As a result
of combustion test, however, it was found that poisonous gases were
removed by flushing with water and heavy metals were condensed into
ash, thus leaving P-oil valuable enough to be utilized as a good
quality fuel oil.

Water-soluble C-oil was collected by the scrubber in the form of
aqueous solution.   When taking the utilization of C-oil into
consideration, it is desirable to collect C-oil with minimum water
content.  Condensation utilizing waste heat made the scrubber able
to collect oil condensed up to 40% by weight of water content.  The
low calorific value of C-oil with 40% by weight of water content was
approximately 1,800 Kcal/kg, which was not too low to prevent
spontaneous combustion of C-oil.  Viscosity was 40 c.p. at 10°C,
which was small enough to permit burning of atomized oil.   Poisonous
elements were S (0.40% by weight), N (0.9% by weight) and Cl (7.90%
by weight).  Heavy metals were Cd (20 ppm), total Cr (2 ppm) and
P (100 ppm).  No Hg and As were detected.  The combustion test proved
that the mixture of C-oil and petroleum fuel oil was satisfactorily
combustible.
                          - 11 -

-------
                                                                     566
4.2  Char and Dust
     Table 4 indicates characteristics  of char and dust.
              Table 4   Characteristics  of Char and  Dust
Analysis item
Industrial
analysis
Chemical
analysis
Grain size
Calorific value
Water content
Ash content
Bulk specific
gravi ty
C (wt %)
H ( " )
0 ( " )
N ( " )
S ( " )
Cl( " )
Char
15
5,500
3.1
30
0.25
70.3
2.7
3.5
2.5
0.06
0.64
Dust
0.05
2,800
4.3
57.5
0.20
45.0
1.9
2.5
1.2
0.3
1.8
Coal (anthracite)
-
6,810
3.5
13.2
-
79.6
1.5
1.3
0.45
0.45
-
     Carbide collected by the fluidized bed is called "char", and that
     collected by the cyclones is called "dust".  The low calorific
     value of char was 5,500 Kcal/kg which is as same as that of coal.
     The low calorific value of dust was 2,800 Kcal/kg which is not
     too small to prevent spontaneous combustion.  Char and dust which
     include volatile matter have good firing property and can be used
     for solid fuel.  Most heavy metal components in char and dust are
     condensed into ash produced by combustion.
                               - 12 -

-------
                                                                  567
4.3  Gas
     Since raw material (waste) is partially oxydized with air, produced
     gas is diluted by nitrogen.  The low calorific value of gas produced
     is therefore as small as 925 Kcal/Nm^, but not too small to prevent
     spontaneous combustion.
4.4  Waste Water
     Since waste water includes trace elements such as sugar,  alcohol,
     organic acid and aldehyde, COD j^ (chemical oxygen demand)  is
     approximately 18,000 ppm and BOD (biochemical oxygen demand)  is
     approximately 22,000 ppm.  Waste water will show acidity  of pH 3
     because of presence of hydrogen chloride which will be generated
     from vinyl chloride and dissolve in water.  Heavy metals, including
     2 ppm of Pb and other less-content trace elements, are negligible.
     Waste water can be treated by current biological, chemical  and
     physical methods such as neutralization, activated sludge treatment,
     cohesion-precipitation, adsorption, etc.
5.   Actions of Harmful Components
5.1  Noxious Gases
     Most noxious elements such as sulfur and chlorine included in  urban
     refuse are converted, after pyrolysis process,  into poisonous  gases
     such as NOx, NH3,  HCN, SOx, H2S and HCl.   Result of measurement  of
     poisonous gases is shown in table 5.
                               -  13 -

-------
                                                                       568
                Table 5    Concentration  of Noxious  Gases
                                                  (Unit:  ppm)
Component of
noxious gas
NOx
S02
H2S
HC1
NH3
HCN
Pyrolysis
reactor
outlet
0-10
15 - 70
0 - 40
70 -150
2-20
20 - 40
Gas cleaning
tower outlet
< 10
< 20
tr
tr
tr
< 1
Incineration
(reference purpose
only)
100 - 500
50 - 100
-
300 - 800
0.3 - 0.5
-
     Every poisonous gas shows  scores  of ppm of  concentration when
     measured at the outlet of  the pyrolysis reactor.   After passing
     through the gas cooling tower, however, their concentration is
     decreased to near zero except for 10 ppiti maximum of NOx and 20 ppm
     maximum of S02-  In comparison with concentration of poisonous gases
     resulting from incineration of refuse,  this pyrolysis process
     features a generation of NOx that is negligibly small.
5.2  Heavy Metals
     Figure 5 indicates the result of actual measurement of distribution
     of heavy metals.

     All heavy metals  were transformed after thermal decomposition into
     char and dust; there was scarcely any transformation into gas and
     oil.  The low-temperature treatment at 500°C adopted by this system
     is effective to prevent scattering of heavy metals, although heavy
     metals are dispersive more in reduced atmosphere than in oxidation
     atmosphere in the case of incineration of refuse.

-------
                                                                              509
^Char    OT] Dust
                                         Water
                                  Oil
                        Gas
          100
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                                             Cr
                 Fig. 5    Distribution of Heavy Metals  in  Products
                                  - 15 -

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                                                                          572
6.   Effective Use of Resources Produced
6.1  Combustion Test of Produced Oil
     Produced oil is favorable to use as fuel oil.   A spray combustion
     test of produced oil was made using a 250 mm ID, 6  m high  cylindrical
     furnace.  The result of test is shown in table  6.

     In this test, P-oil was burnt independently, while  C-oil was  burnt
     as a mixture with petroleum fuel oil.  Stable combustion was  obtained
     at 1400°C of maximum temperature and 700°C of furnace outlet
     temperature.  On making a comparison among petroleum fuel  oil,
     P-oil and C-oil concerning generation of noxious gases;  concentration
     of NOx was 90 ppm, 125 ppm and 430 ppm,  respectively.   Concentration
     of SOx was 250 ppm, 10 ppm and 150 ppm,  respectively.   Concentration of HC1
     and Cl2 was 0 to 20 ppm for fuel oil and P-oil,  while concentration
     of HC1 and Cl2 was 2000 ppm and 30 ppm,  respectively,  for  C-oi-1.

     As mentioned above, P-oil can be evaluated that it  is  roughly
     suitable for fuel oil.   C-oil can be used for fuel  oil when it is
     mixed with petroleum fuel oil, although  generation  of  relatively
     high concentration of chlorine must be taken into careful  consideration.
6.2  Combustion Test of Char
     Char which is similar in characteristics  to coal  can be  used  for
     solid fuel.  A combustion test of  char was  made using  a  300 mm ID,
     5.5 m high turning-injection type  fluidized bed furnace.   The result
     of test is shown in Table 7.

     Sufficient combustion was obtained at 2.1 of coefficient of excess
     air and at 800°C of furnace temperature.  Although  exhaust gas
     included noxious gases such as 5 ppm of CO  and 50 ppm  of NOx,
     neither H2S nor SOx were generated.   Dispersion of  heavy tnetals was
     negligibly small after washing.  Although combustion test of  dust
                               -  17  -

-------
                                                                 573
     has not yet been made,  it  is  assumable  that approximately the  same
     result as of the combustion  test  of  char will be obtained.

     As mentioned above,  char can  be evaluated to be useful solid fuel
     to apply to pre-combustion of excess muddy substances in raw material.

     As a whole, produced gases are combined with other  fuels and are
     used for heating drying air  and for  generating steam.  P-oil which
     is high in calorific value can be burnt in boilers  using the same
     handling manner as conventionally used  for fuel oil.  C-oil which
     is low in calorific  value  can be  used without special problem  by
     mixing it with  petroleum fuel oil, etc.  Specially, use of a triple-
     fluid type oil  burner permits spray  combustion of C-oil without
     mixing it with  other fuel.  Char  and dust can be burnt in a fluidized-
     bed combustion  furnace.  Heavy metals,  most of which are transferred
     into char and dust after pyrolysis process, can be  prevented from
     scattering into the  atmosphere because  they are finally condensed
     in ash by fluidized-bed combustion.
7.    Ease of Operation  and  Control of Pyrolysis Reactor
     In putting the  urban wastes pyrolysis plant into practical use,
     it is essential to make  the pyrolysis reactor easy  to operate  and
     control.   Figure 6 shows variation of reactor temperature with  time
     and figure 7  indicates fluidized-bed temperature with time.

     Fluidized-bed temperature is stabilized at 500° +20°C while  loss
     of fluidized-bed pressure is stabilized at 550 mm 4-150  mm Aq.
     Although fluidized-bed temperature can easily be varied with either
     quantity of supply of  waste or  quantity of supply of air, the  latter
     is superior to  the former in speed of response to the requirement
     of control.
                              -  18  -

-------
                                                               574
             Reactor
               outlet i
            Cyclone
               inlet
Fluidized
  bed
                     400
                     Temperature (°C)
         too
Fig.  6   Variation of Fluidized-bed Temperature with Time
            r
                               -Vj' ' Fluidized
                               11 *  '    bed
                                2.i'Fluidized bed
                                TV!*  + Dispersion plate
                      .»

                              ^f
          o i-
                     •rV
                Pressure loss (mm Aq)

Fig. 7   Variation of Fluidized-bed  Pressure Loss with Time
                        -  19  -

-------
                                                                  575
     In this pyrolysis  method,  heat  usable  in  the  pyrolysis  reactor  is
     limited to only partial combustion  of  waste and,  therefore,  it  is
     possible to assume that pyrolysis  temperature simply  depends on
     usage of combustion heat.   An example  of  heat balance around the
     pyrolysis reactor  is shown in figure 8.
Calorific
value
Heat
balance

Combustion heat Qg
/
Sensible
heat of
water
Qaq
Sensible heat
of waste Qw
Heat loss
Ql
Heat of
decomposi-
tion
Qc
Sensible
heat of
air
Qair
r
	 1 	 L 	 L.. . 	 	 1
Sensible
heat of sand
,V
                      20
60
80
                                                                    100
         Fig. 8   Heat Balance around Pyrolysis Reactor
     The heat balance is formularized as follows:
     QB -

                                                                  (i)
     Each item in the formula (1) can be represented by quantity of
     supply of waste W (kg/h), quantity of supply of air Qair (kg/h),
     quantity of supply of sand Qs (kg/h), moisture content Raq (-) ,
     plastic content Rp (-), paperwaste-and-garbage content Re (-) ,
     pyrolysis temperature T (°C) and inlet temperature t (°C).
     The  following  formula can be induced by adjusting and approximating
     the  formula (1) about pyrolysis temperature  (T):
                                -  20  -

-------
                                                            576
       760 (1-Ls) Gair-(600 Rag + 85 RC + 282 Rp) W
         0.2 Gair + (0.3 - 0.7 Raq) W  + 0.2 Gs
                                                    (2)
Using formula (2) , it is possible to set operating condition of the
pyrolysis reactor and to properly transfer the operating condition
to compensate for any variation of pyrolysis temperature.   Values
possible to control in the pyrolysis reactor are quantity of air,
quantity of waste and quantity of sand to be supplied to the reactor.
When target value of pyrolysis temperature (500°C) drops AT, for
instance, the original temperature can be recovered by varying quantity
of air supply by AGair = AT/(9T/3Gair) W1.Gs or by varying quantity
of waste supply by AW = AT/(3T/3w') Gair. Gs.  (See figures 9 and
10.)
                                Supply of waste W': constant
                         6
Fig. 9
Fig. 10
Variation of Decomposition Temperature with Air
Quantity
                                	>  g  x  Supply of air Gair:
                                 Quantity        x      constant
                                 of raw material
 Variation of Decomposition Temperature with Quantity
 of Rail? Material
                          -  21  -

-------
                                                                   577
     Precise estimation of  operational factor AGair or AW is possible by
     obtaining values  (3T/3Gair) and  (3T/3W*) as the result of pyrolysis
     temperature control test  using the small-sized pilot plant mentioned
     before.

     Total operating time of the 500  mm dia. pyrolysis reactor has already
     reached 1500 hours, including 200 hours of continuous operating time.
     Through this period of operation, it was proved that the fluidized
     bed pyrolysis system is superior to other systems in operational and
     control function.
8.    Conclusion
     The outline of  the  fluidized bed pyrolysis process described above
     is  listed as follows:

     (1)  Treating urban wastes by pyrolysis process at a temperature
          as  low as  500°C permits high-yield recovery of plastic oil
          of  7,300 Kcal/kg in  calorific value and cellulosic oil of
          1,800 Kcal/kg  (at  40 wt % of water content) in calorific value.
          Plastic oil  can be used instead of petroleum fuel oil.
          Meanwhile, cellulosic oil can be mixed with petroleum fuel oil.
     (2)  By-products  recovered from urban wastes are char of 5,500 Kcal/kg
          in  calorific value and dust of 2,800 Kcal/kg in calorific value.
          Char can be  utilized instead of coal #nd dust can also be used
          for low-class  solid  fuel.
     (3)  Noxious gases  such as HC1 and H2S can easily be removed by
          flushing with  water.  Because of low-temperature treatment, NOx
          scarcely generates.  Because of low-temperature treatment, most
          heavy metals are transformed into char and dust after thermal
          decomposition  and  finally condensed into ash.
     (4)  The fluidized  bed  pyrolysis reactor is superior to other
          reactors in  operational and control function.
                              -  22  -

-------
                                                                      578
                           Fluidized Bed Pyrolysis
                         Discussion Leader:  Mr. Hideaki Takamatsu
Question:  Does this unit operate on only separated paper and plastic

           or can it operate on the entire waste stream?

Answer:    This installation is designed to recover oil as a fuel after

           paper and plastics are separated from mixed municipal waste.

           In other words  this system cannot directly have mixed waste

           thermally cracked.  This is because typical mixed collected

           waste in Japan contains things which are not subject to

           thermal cracking,  such as galss jars,  iron scraps  masonry

           products and high water content materials,,  such as garbage

           and bulky waste.

Question:  What is the size?  Is it commercially viable or just a

           piloc plant?

Answer:    I don't remember the exact figure,  but I think it will be

           1500 to 2000 millimeters.  In the past we started out with

           a bed with an 80 millimeter diameter and got into one with a

           500 millimeter diameter with 200 hours of continuous operation.

           In total,  we have operated the installation for 1500 hours al-

           together.   As to the plant we are thinking of building, we have

           finished the code test with that equipment.  The plant is a

           pilot plant to establish the technology to set up an actual

           and operating plant in terms of design,  construction and

           op?raiion.

Question:  How are the organics separated from the waste stream?

-------
                                                                   579
Answer:    We separate garbage which is later subject to methane fermen-




           tation.  The rest of the organic material is thermally




           cracked into fuel.  I don't have any statistical data,




           however, if you would like it, I can have some data such




           as the material balance sent to you.

-------
                                                          580
5.  PYROLYSIS
   5-4  R § D for High-Temperature Melting of



        Incombustibles and Refuse Unfit for



        Incineration
                   Planning  Division



             Bureau of  Public  Cleansing



            Tokyo  Metropolitan Government

-------
                                                              581
                             Contents








Introduction




1. Experiment




   1.1  Objectives




   1.2  Research items




   1.3  Period of experiment




   1.4  Outline of experiments






2. Outline of experimental equipment




   2.1  Design factors and specifications




   2.2  Process flow-sheet






3. Experimental results




   3.1  Results of preliminary experiments




   3.2  Results of experiment in the.first half of the experimental




        period








Conclusion
                              - 1 -

-------
                                                               582
 Introduction




     Since  1973, Metropolitan Tokyo has collected refuse classified




 by  type  to  prevent incinerator pollution  (secondary pollution) and




 protect  the incinerator itself.  The solid wastes which are collected




 on  this  classified basis are metals, glass, ceramics and other




 incombustibles, as well as plastics, rubber, leather and other refuse




 unfit for incineration.  Together, they amounted to approximately




 3,800 tons  per day in 1978.  In the absence of suitable processing




 techniques, however, these solid wastes have been dumped or used for




 reclamation without processing.




     Hence  the need is being felt to devise a new processing tech-




 nique which can process classified refuse without secondary pollution




 while meeting social needs for turning refuse into useful end-products




 and contributing to efficient use of landfill area.




     In  this situation, the Tokyo Metropolitan Government in November




 1976 concluded an "agreement on provision of experimental facilities




 for the  development of classified refuse processing technique" with




 the Plastic Waste Management Institute and Nippon Steel Corporation,




 in order to devise a useful method of processing classified refuse.




 Based on this agreement, experimental high-temperature melting/




 processing equipment was delivered to the Tokyo metropolitan au-




 thorities in January 1978.




     This progress report concerns the results of tests on the ex-




perimental plant.
                               - 2 -

-------
                                                              583
 1.  Experiment




 1.1  Objectives




      The  experiment was  aimed at developing  a  refuse  disposal  tech-




 nique to  mainly  process  classified  solid wastes  and at  devising  an




 optimum system by which  this technique can be  turned  to practical




 use.   The objectives of  the experiment were:




 (1)   Prevention  of secondary pollution




 (2)   Utilization of solid wastes as  "resources"  and landfill




 (3)   Establishment of highly reliable and very efficient technique




      of refuse disposal






 1.2   Research items




      To attain the above objectives, the following research items




were  set.




 (1)   Processing  performance




 (2)   Operating costs and optimum operating conditions




 (3)   Reliability and safety




 (4)  Properties of pollutants discharged from the system




 (5)  Methods of utilizing incineration products






1.3  Period of experiment




     The  period of the experiment is from January 1978 to March 1979




and is divided into the following three phases.




(1)    Phase 1     Preliminary  experiment      January - March 1978




(2)    Phase 2     Major experiment            April 1978 - Jan. 1979




(3)    Phase 3     Follow-up experiment         February - March 1979
                               - 3 -

-------
                                                                584
 1.4  Outline of experiments




      Experiments during the experimental period can be  outlined as




 follows:




 (1)  Phase  1




          Preliminary  experiments  are  conducted to  obtain  the basic




      data necessary  for planning of  the  major  experiments  to follow.






 (2)  Phase  2




          On the basis  of  the preliminary  experimental  results,  long-




      term continuous experiments are conducted en classified refuse.






 (3)   Phase  3




          In order to  further substantiate the results  of  the major




      experiments, follow-up  experiments  are conducted on the pro-




      cessing of  solid wastes other than  classified  refuse.









 2.  Outline of experimental equipment




 2.1  Design  factors and specifications




 2.1.1  Properties of refuse




     As standard solid wastes for use in the experiment, refuse with




 properties as shown in Table 1 was chosen in compliance with the




 results of classified refuse property research conducted by the Tokyo




metropolitan authorities in fiscal 1974.
                               - 4 -

-------
                                                                585
             Table 1  Properties of classified refuse

                                     (Weight percentage on wet basis)
Combustibles
26.8
Refuse unfit for
incineration
21.9
Glass, ceramics
34.7
Metals
16.6
2.1.2  Processing capacity

     The processing capacity of the equipment is 40 tons per day in

terms of the classified refuse with properties as given in Table 1.
2.1.3  Submaterial consumption

(1)    Coke           108 kg/ton-refuse
Heat source of melting
furnace

For slag fluidization

Blast oxygen enrichment

Combustible gas purge

Concrete solidification
of residuals
2.1.4  Environmental pollution prevention performance

     Table 2 shows equipment performance in terms of removal of

pollutants from discharges.
(2)
(3)
(4)
(5)
Limestone
Oxygen
Nitrogen
Cement
240 kg/ton
45 Nm3/hr
100 Nm3/d
2,340 kg/d
                               - 5 -

-------
                                                                  536
               Table 2  Pollutant removal performance

Gaseous
wastes
Solid wastes
Pollutants
Soot and dust
sox
NOX
HC1
Slag
Concrete-solidified
/briquette
Calculated values
3
O.lg/Nm & under
70 ppm & under
100 ppm & under
100 ppm & under
Usable for landfill
Usable for landfill
 2.1.5   Recovery  of material  sources




 (1)  Thermally  cracked-gas:   This  can be  effectively  used as  fuel.




 (2)  Iron                  :   This  is reusable.






 2.2  Process flow sheet




     Fig. 1 shows the process  flow sheet of  the  test plant.




     Together  with coke and  limestone, classified  (assorted) refuse




 is charged into  a vertical melting furnace (9) to  go through pro-




 cesses  of drying, thermal cracking, combustion,  and melting.  In this




 operation, paper and other combustibles, as well as plastic, leather




 and  other refuse unfit for incineration are  thermally cracked and




 withdrawn at the furnace top as combustible gases.




     Glass, metal and other incombustibles are melted and discharged




 through the slag notch in the  furnace bottom into  a slag ladle car




 (10) for transfer to the slag  treatment yard (8).  Upon cooling, the




melt is separated into iron and slag for separate  trip out of the




 system.
                               - 6 -

-------
                                                                        587
      The  combustible gas  from  the  furnace  top is  cleaned of noxious




 substances  and oil  contents by dust catcher  (11), venturi scrubber




 (12), and mist separator  (13), and emerges as a  fuel gas, part of




 which is  then burned in a hot  stove (16),  as a heat source for the




 melting furnace, the remaining gas being burned at a flare stack  (15)




 for discharge into  the atmosphere.  With this practical model, energy




 is recovered for use in boilers, etc.




     On emerging from the venturi scrubber (12) and mist separator




 (13) after  serving  to wash combustible gas, wash water is led into the




 circulating wash water treatment plant (21) to be cleaned of oil




 contents  and suspended solids, after which the water is recirculated




 to the venturi scrubber and mist separator as wash water.  Meanwhile,




 the removed oil contents and suspended solids are fed into the melting




 furnace (9) in a state of tar-sludge mixture for processing with




 refuse.




     The  small amount of recirculating wash water extracted from the




 circulating wash water treatment plant (21),  plus dust from the dust




 catcher (11) are delivered to waste water treatment plant (22) for




drying and subsequent incineration.  The ash from incineration is




processed into concrete-solidified briquette by the concrete solidi-




 fication equipment  (23)  and is land-filled.









 3. Experimental results




 3.1  Results of preliminary experiments




     In preliminary experiments conducted between January and March




1978,  the  experimental plant was examined for its refuse processing

-------
                                                                   588
 capacity,  operational conditions  and pollution preventing performance,




 etc.,  thus providing basic data for planning the experimental period.




     During this period,  in which the experimental  plant  was  operated




 for approximately 1,000 hours,  the following information  was  obtained.







 3.1.1   Refuse processing  capacity




     Classified refuse processing capacity  is  40 tons per day.   Com-




 pared  with the capacity of other  equipment,  the capacity  of the




 melting furnace is so excessive that the  functional balance of the




 entire equipment is lost  to render stable operation difficult.




     Accordingly,  to  stabilize  operation, the  plant capacity  must be




 balanced by  decreasing the furnace diameter  to an extent  where furnace




 capacity is  optimized.







 3.1.2   Submaterial consumption




     The consumption  of coke -  whose  effects upon operating costs are




 the  greatest  of  all submaterials  used  - has exceeded calculated values




 on account of the  stability of  furnace conditions having been given




 top  priority  in  the initial stages  of  the experiment and because of




 the  level of  slag  temperature control having been raised.






 3.1.3  Pollution prevention performance




     As concerns pollutants in waste gas,  nitrogen oxides  may exceed




 calculated values but in terms of control  values for incineration,




 they are drastically lower than the calculated values.   Soot and  dust,




hydrogen chloride and sulfur oxides are within the calculated  values.

-------
                                                                 589
     As regards slag and concrete-solidified briquette, they have




passed the official standard for landfill (titled the "Criteria on




Deletirious Industrial Wastes") and are therefore usable for land-




fill.







3.1.4  Recovery of resources




     Recovered gas can be effectively reused within the plant as




fuel.  Recovered iron can also be recycled.







3.1.5  Operational conditions




     Of all operation conditions, the most important is blast volume,




which is optimal at approximately 1,600 Nm /hr.







3.2  Results of experiment in the first half of the experimental




     period




     In this experiment, the melting furnace diameter was  decreased




and other necessary modifications were made to the equipment before




the experiment was restarted in June 1978.  Experiments in the first




half ended in early September.   During this period,  the experimental




equipment was operated for approximately 1,600 hours to determine




the capacity of post-improvement equipment,  for the effects of blast




oxygen concentration,  etc.   The following information was  obtained




from this experiment.







3.2.1  Processing capacity




     The experimental  equipment can be stably operated to  process




45 - 50 tons of classified refuse per day.

-------
                                                                   590
 3.2.2  Submaterial  consumption




     Coke  consumption is approximately 110 kg per ton of classified




 refuse.




     At a  blast oxygen concentration of approximately 30 percent,




 coke consumption will be reduced to about 80 kg per ton of classified




 refuse.







 3.2.3  Pollution prevention performance




     Pollutants in  a waste gas have the following composition, which




 falls below calculated values in each of the items given.




                  Soot and dust          87 mg/Nm




                  Hydrogen chloride      15 ppm




                  Nitrogen oxide         58 ppm




                  Sulfur oxide           7.4 ppm







 3.2.4  Resources recovery




     A little more  than 30 percent of the gas generated is reused as




 fuel for the hot stove of the experimental equipment.  The remaining




 gas can also be a source of energy.  Iron can be recycled as materials




 for weights etc., and has the utility value equaling that of scrap




 iron.




     Slag can be utilized as landfill.   With the progress in develop-




ment of slag utilization technique in the Japanese steel industry,




 slag may be granulated or otherwise processed into building materials




 or many other end-products.

-------
                                                                   591
Conclusions




     The preliminary experiment and the early half of the main ex-




periment have proved that this high-temperature melting of classified




refuse is a. low-pollution type processing technique capable of




recovering combustible gases and iron from incombustible solids.




     Further studies are yet to be made,however, concerning higher




economic efficiency, reliable operating technique and more effective




slag utilization.




     The following experiments will therefore be made in the future.




(1)  Development of slag utilization technique




          To ascertain the feasibility of effective slag utilization,




     a variety of civil engineering tests will be conducted.  New




     water-granulating equipment will also be installed, so that




     further experiments may be made to find the means of multiple




     utilization of slag.






(2)  Improved economic efficiency




          Tuyeres will be improved and any resultant reduction in




     coke consumption will be confirmed in tests to achieve higher




     economic efficiencies.






(3)  Long-term continuous operation




          Long-term continuous  operation will be made  to verify equip-




     ment reliability and safety and to  establish operating technique.




          It  should be  added  that  this is  a  progress  report,  and




     results  are  subject to  change depending on  results  of  future ex-




     periments .
                              - 11 -

-------
                                                                       592
                      (Fig.l)  Process flow sheet
 1), 2), 3) Hoist crane,

 4) Submaterial pit

 5) Submaterial hopper

 6) Classified refuse

 7) Hoist crane

 8) Slag treatment yard

 9) Melting furnace

10) Slag ladle car

11) Dust catcher

12) Venturi scrubber

13) Mist separator

14) Exhaust blower

15) Combustion-emission
    tower
16) Hot stove

17) Hot stove stack

18) Blower

19) Raw water pit

20) Cooling water pit

21) Circulating wash water treatment
    plant

22) Waste water treatment plant

23) Concrete solidifying equipment

24) Clean water tank

25) Administration Office

26) Boiler
 A)  Classfied refuse

 B)  Submaterial

 C)  Out from the system

 D)  Clean water

 E)  Process  water

 F)  Steam for hot water service

 G)  Return to furnace

 H)  Hot  blast main

 I)  To  venturi scrubber
 J)  Dust

 K)  to  plant

 L)  Steam

 M)  Boiler  water,  Sanitary water
    for use in the plant

 N)  to  Flare  stack

 0)  Out from  the system
                               - 12 -

-------
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-------
                                                                            595
                        R and D for High Temperature
                        Melting of Incombustion a;id
                        Refuse Unfit for Incineration
                        Discussion Leader: Mr. Naomichi Hirayama
Question:  The high temperature melting furnace and system  appears to
           be similar to two U.S. systems tried in the late 1960's and
           early 1970's.  Do you have the benefit of the U.S. reports
           on systems we called "The Melt-Zit" unit and  The Andco-
           Torrax unit?  (These reports should be available and may be
           of assistance.)
Answer:    I am one of the members of an Advisory Committee on this
           matter for Tokyo City.  Yes,  I have the benefit of reading
           these two documents concerning these two systems—both the
           "Melt-Zit" and the  'Andco-Torrax:.   As I mentioned before,
           there are two different factors of the system developed
           by the Plastic Waste Management Institute and the Nippon
           Steel Corporation,  In other words, these two units devel-
           oped by the United States are sort of in competition with
            he one developed by the Plastic Waste Management Institute
           and Nippon Steel Corporation.

-------
                                                                   596
                       SUMMARY COMMENTS




                     JAPANESE GOVERNMENT




                Mr.  Tadayuki Morishita, Japan Chairman






           At this meeting we have dealt with landfill issues, resource




recovery through thermal cracking and pyrolysis.  The way this conference




has been managed, we have exchanged reports in advance; and questions




to those reports have been available ahead of time.  This procedure en-




abled us to have a very efficient exchange of information and also




very informal, frank discussions in a very limited amount of time.




           Since the third conference which was held in 1976, both coun-




tries have experienced changes in population and legislation, including




some  progress in the field of solid waste management.  So I think that




this conference was held at the right time in order to exchange informa-




tion concerning problems related to solid waste management.




           I think the meeting was very, very useful. I found that




even though there were quite different problems—differences in land




area and differences in resources, I think we do share the same pro-




blems concerning landfill  practices and consumer waste in the field of




solid waste management.   I have been impressed by the United States




approach to resource recovery of waste from the viewpoint of resource




conservation which is authorized by RCRA.   However, in Japan, at




this point in time,  solid waste management must be approached from




the viewpoint of reduction of waste before final disposal.  I feel that




the Japanese should make more effort in the area of waste reduction.

-------
                                                                   597
           As to technology related to pyrolysis, I understand that




in the United States, the technology is not well-developed yet.  However,




in Japan we need pyrolysis or similar technology in order to control




air and water pollution as part of our overall solid waste management




program.  I think there are some very promising developments  in




terms of implementing pyrolysis technology. For example, in 1978,




we started construction on two pyrolysis plants and by 1979 we are




planning to build two different systems.  Therefore, as we develop these




two systems I would like to provide you with some information about




them, including the economic engineering, pollution and other assessments.




           As to the assessment and management of landfill sites, we




have general funds and guidelines in both countries.  I think there is




a need to detail these guidelines and standards.  In order to do so,




I feel there is some need for an information exchange such as this




conference provides.  This kind of conference concerning solid waste




management is very useful and meaningful for our future actions.  Be-




ginning tomorrow we will be visiting project sites in your nation and we



are hoping to get some concrete information through these visits.




           As a last remark,  I would like to thank our Chairman, Dr.




Skinner, and other delegates from EPA for their effort to make this




conference operate very smoothly.  Also 1 would like to mention some




thanks to the American Public Health Association including Ms. Davidson




and her staff.  We are very grateful to them for providing us a place




for our conference.  And to the delegates from both sides I would




like to say thank you so much for your cooperation.

-------
                                                                              598
     Dr. John Skinner, U.S. Chairman, then gave his summary comments



after which the Joint Communique was presented to the delegates.  Chairman



Morishita then presented these additional and final remarks.








     I'd like to make some additional remarks about the Joint Communique.



At this up-coming fifth conference, we Japanese would like to show our




American guests some of the facilities in our country that we discussed



at this meeting.  Because of the American interest in industrial and haz-



ardous waste management, which Dr. Skinner mentioned,  I also would like



to show our guests some of our Japanese facilities for disposing of these



wastes.  These are some of the additional topics which we might include



for discussion at the fifth United States-Jqpan Conference.  I hope that all



of the delegates in attendance at this meeting will be able to attend the



upcoming fifth conference in Japan.

-------
                                                                  599
                     SUMMARY COMMENTS

                     U.S. GOVERNMENT


                Dr. John  H. Skinner, Chairman
           On behalf of the United States Environmental Protection

Agency, I would like to make a few summary remarks.  First, I would

like to thank Mr. Morishita for his able chairmanship and for his

very interesting paper on Solid Waste Management in Japan.  It's

very pleasing to hear that we are both moving toward higher levels of

solid waste control in order to protect the environment.

           Second, I wish to thank Mr. Namiki for his excellent paper

on the value of pneumatic conveying systems which hold promise for

safe, clean,,and quiet transport of solid waste.  I would like to

thank Dr. Kawaguchi for his paper on location of refuse treatment

facilities and for pointing out the difficulties of siting facilities.

The public opposition which he indicated Japan faces is similar to

our problems in the United States. We  want to express appreciation

to Mr. Miyanohara for his discussion of the difficulties associated

with the design and operation of systems for the removal of HCL in

incinerator plants.

           We, the United States delegation, are especially appreciative

to Dr. Tanaka for his very comprehensive analysis of the overall environ-

mental impact on solid waste management systems and his perspective

on the establishment of a methodology for, hopefully, balancing the

trade-off of the various environmental impacts.  We want to thank
                                           &
Dr. Yagome for his paper on Leachate Treatment at Solid Waste

Disposal  Sites and his complete delineation of all of the

-------
                                                             600
factors that need to be considered related to this issue.   This will be



very helpful as   leachate treatment becomes more prevalent in the



United States as a result of our control efforts.



           Mr. Morishita's and Dr. Tanaka's comments on recycling



municipal wastes in Japan including refillable bottles, paper



recycling, source separation and separate collection, were very



interesting and helpful.  I was most interested in Mr. Mitani's paper



on the Effective Use of Waste Heat of Refuse Incineration  in Sapporo



City.  Dr. Naito's paper on Composting Systems was very informative,



especially since composting of municipal solid waste in Japan seems



to be successful while in the United States we have not had very



much success with it.          (



           Mr. Takamatsu gave several interesting papers—one on



research and development of a promising experimental selection polar-



izing glassifier and two papers on fuel gas production through two-



bed pyrolysis and fluidized bed pyrolysis.  Hopefully by reviewing



these papers we can see some of the differences and prospects for



success for pyrolysis in Japan as compared with the United States.



I would like to thank Dr. Hirayama for his paper on High Temperature



Melting of Incombustion and Refuse Unfit for Incineration.  We know



of one incinerator where the burning of film destroyed the neck of



the incinerator due to the high temperature.



           We were also very pleased to meet and talk with our



three observers from Japan, Dr. Urata, Mr. Ota and Mr. Uemura.  Finally,



I'd like to thank Mr. Uyama, our able translator, for his fortitude



over the last few days in keeping up with us and for providing a

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                                                                   601
very excellent translation.



           On behalf of the U.S. delegation, I would like to make just



one additional comment before closing.  I think this has been a very useful



exchange of information.  I'd like to point out that the solid waste



program in both nations is changing and that we will probably  be




moving toward industrial and hazardous waste management to a far



greater  degree than we have in the past.  I think there will be a



need for an exchange of information on those subjects as Chairman



Morishita mentioned, as well as on municipal waste which was the



focus of this conference.



           Also, I would like to echo Mr. Morishita's thanks to the



American Public Health Association and to Ms. Davidson and her staff



for the fine management of the conference'over the past two days.



           I offer you my best wishes on your tour of the facilities



over the next 10 days.  Mr. Thompson will be accompanying you on



most of the tours.  He will pick you up tomorrow morning at 8:30 a.m.



for your trip to the Beltsville Sludge Composting Plant.  One of the



projects that you will be visiting is the Mountain View Methane Gas



Recovery facility in San Francisco.  This is an innovative project on



the recovery of combustible gas from a landfill and appears to be



successful.  This is one  of the projects that we have .been involved




with over a number of years.  I have copies of a paper on the gas



recovery facility which my staff has prepared and I will make it available




to you.  You may want to read it before you visit this facility so



that you can place the project in its proper perspective.

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                                                               602
                  THE FOURTH U.S.- JAPAN GOVERNMENTAL
                 CONFERENCE ON SOLID WASTE MANAGEMENT

                     WASHINGTON, D.C.
                     March 12-13, 1979

                SUMMARY OF RESULTS AND CONCLUSIONS

           The Fourth U.S. - Japan Conference on Solid Waste Management
was opened with the welcoming speeches by Dr. J. Skinner, E.P.A.
Director, Land Disposal Division and Mr. T. Morishita, Director,
Solid Waste Management Division, Water Supply and Environmental
Sanitation Department, Environmental Health Bureau, Ministry of
Health and Welfare.
           At this conference, reports on the following subjects were
submitted and discussed.  (l)  Status reports of solid waste management,
(2) reports concerning environmental assessment for landfill disposal,
(3)  papers on leachate control and treatment and (4) reports on
resource recovery technologies.
        In preparation for the conference, the papers and important
discussion questions on papers prepared by the other country were
exchanged between two countries before the formal meeting.  Thus,
the conference had fruitful information and frank opinions exchanged
efficiently between the nations in a limited time of two days.
On the first day, Dr. J, Skinner was the chairman and Mr. T. Morishita
was the chairman for the second day.  Presentations and discussions
were conducted on all prepared papers.
           The status of the solid waste management and special subjects

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                                                               603
were reported and opinions were exchanged mainly by answering the




questions prepared before the meeting.  Following are some primary




points of the meetings.




           After the third Japan-U.S. Conference on Solid Waste Manage-




ment in 1976, it was found that regulations and policies on solid waste




management were improved and progress made in both nations.  It was




recognised that  although the availability of the land and natural




resources in both countries are quite different, problems on solid




waste management, for example, siting of landfills or post consumer




waste problems are common.  Discussions concerning resource recovery




from solid waste, indicate that at the present time, in the U.S.A.,




they recover resources from waste in terms of resource conservation




under RCRA and in Japan they conduct resource recovery in terms of




reduction of waste to be disposed of at final disposal sites.   In




papers reporting on environmental assessment and management for land-




fill disposal, general criteria and drafts of guidelines were prepared




for both countries.   For the future, more specific and detailed guide-




lines should be prepared and participants thought it might be




useful to exchange information on individual landfills presently in




operation.   Results of pyrolysis technology discussions indicated




they may not be ready for commerical useage in U.S.A. but pryolysis




may have some potential usage in terms of pollution control,




especially air and water pollution control after waste processing.

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                                                                    604
     The presentation and discussion in each subject are as follows:




I.  U.S.-Japan Status Reports.




     Mr. J. Thompson and Mr. T. Morishita presented status reports




on solid waste management in general in their countries.  Mr. Namiki,




Dr. Kawaguchi and Mr. Miyanohara submitted the papers on specific




projects, pneumatic conveying systems, location problems and HCL




removal in incineration plants.  Mr. G.A.  Garland reported on "State




Solid Waste Management Plans", one of the guidelines prepared by




E.P.A.




II.  Environmental Assessment for Land Disposal




     Mr. T.V. DeGeare Jr. discussed "Guidelines for the Landfill




Disposal of Solid Waste" and Dr. M. Tanaka presented the summary




report on environmental assessment from the view of the solid waste




management.




III. Leachate Control and Treatment




     Mr. B. Stall and Dr. K. Yagome presented and discussed leachate




treatment based on experimental data.



IV.  Resource Recovery Technologies




     Dr. M. Tanaka presented a general view of the effective usage of




solid waste in Japan.  Mr. H. Mitani and Dr. S. Naito reported on




specific topics, waste heat recovery and composting respectively.  Mr.




A. Peter Jr. and Mr. D.B. Sussman reported on special resource recovery




topics; markets for recovered materials and the recovery of energy




from municipal solid waste respectively.  Mr. H. Takamatsu and Dr.




N. Hirayama submitted papers on resource recovery technologies, with




special emphasis on pyrolysis.

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                                                                          605
 During the discussion, it was found that both countries face the




difficulties of siting solid waste management facilities for landfill




disposal as well as resource recovery.  Therefore  it was recognised




that research on how to secure necessary land for  solid waste disposal




with considerations of environmental pollution control and obtaining




consensus of surrounding habitants and exchanging  of this information




is highly desirable.




     Discussions of landfill disposal indicated that many landfills




are not properly operated and maintained.  Research on leachate treat-




ment is needed for correction of improper landfill operation and to




prevent environmental pollution in the future.  These actions are




necessary in order to obtain land for waste disposal facilities.




     In the area of resource recovery, it was pointed out that both




countries have their own unique problems, and therefore the system




failure in one country does riot mean the failure in other countries.  It




was found that economic factors in the U.S.A. and  environmental factors—-




in Japan are highly weighted repectively.




     Both countries face serious hazardous waste problems and they may




haue to concentrate their efforts on countemeasures to protect the




environment from hazardous waste.




     The conference was closed with the hope  that  the technical research




cooperation between Japan and the U.S. in the area of solid waste management




will be promoted under the leadership of Mr. K. Kunihawa and Dr. J. Skinner.




Mr. J.  Thompson and Dr. M. Tanaha will serve as windows or coordinators in




their countries for this technical cooperation.

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                                                                606
     As one of the concluding actions of the Fourth United States




-Japan Governmental Conference on Solid Waste Management,  the two




Chairmen presented the Joint Communique to the delegates.








        THE FOURTH U.S. - JAPAN GOVERNMENTAL CONFERENCE




               ON SOLID WASTE MANAGEMENT




            Washington, D.C.       March 13, 1979






                   JOINT COMMUNIQUE




     The Fourth U.S. - Japan Conference on Solid Waste Management




was held in Washington, D.C. March 12, and 13, 1979.




     The Japanese delegation, headed by Mr. Tadayuki Morishita,




Director, Waste Management Division, Water Supply and Environmental




Sanitation Department, Environmental Health Bureau, Ministry of Health




and Welfare, was composed of four national government officials and




two local government officials, four various representatives from



research and training institutes and three observers.




     The. U.S. delegation, headed by Dr. John Skinner, Director




of the Land Disposal Division, Office of Solid Waste, U.S. Environmental




Protection Agency, was composed of 10 EPA officials and various repre-




sentatives from other Federal agencies and public interest groups.




     Dr. Lewis Hughes, Deputy Associate Administrator for Inter-




national Activities, greeted the Japanese delegation on behalf of the




Administrator and delivered remarks of welcome.




     In addition to the conference in Washington, the Japanese delegation




will visit eight innovative solid waste management and resource recovery

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                                                                      607
projects in Washington, D.C.,  New York, New Orleans, Vicksburg,

Phoenix and San Francisco areas.

     The U.S -Japan   Conference on Solid Waste Management grew out

of the U.S. Japan Ministerial  Conference on Environmental Pollution

Control held in Washington, D.C. in June 1971.  Continuation of an

exchange of information on environmental concerns in both nations

was assured by signing of a formal agreement in 1975.  The First

Conference on Solid Waste Management was held in Tokyo in 1973, the

second in Washington in 1974 and the third in Tokyo in 1976.

     During the 1979 Conference, the two delegations presented nineteen

papers and exchanged information on various aspects of the solid

waste problems confronting each country.  Principal subject areas

were Environmental Assessment  for Land Disposal, Leachate Control

and Treatment and Resource Recovery Technologies.  The discussions

were vigorous and both sides agreed that the exchange was very useful

in making contributions to mutual understanding between Japan and the

U.S. and promoting new areas for research and study.

     The conference agreed to  continue information exchanges in

technical and program areas and work toward problem areas of mutual

interest.  The conference agreed to consider a fifth conference,

perhaps late in 1980 in Japan.
                                                                 ya 1842
                                                                 SW-789

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                          EPA  REGIONS
U.S. EPA, Region 1
Solid Waste Program
John F. Kennedy Bldg,
Boston, MA 02203
617-223-5775

U.S. EPA, Region 2
Solid Waste Section
26 Federal Plaza
New York, NY  10007
212-264-0503

U.S. EPA, Region 3
Solid Waste Program
6th and Walnut Sts.
Philadelphia, PA 19106
215-597-9377

U.S. EPA, Region 4
Solid Waste Program
345 Courtland St., N.E.
Altanta, GA 30308
404-881-3016
U.S. EPA, Region 5
Solid Waste Program
230 South Dearborn St.
Chicago, IL 60604
312-353-2197

U.S. EPA, Region 6
Solid Waste Section
1201 Elm St.
Dallas, TX 75270
214-767-2734

U.S. EPA, Region 7
Solid Waste Section
1735 Baltimore Ave.
Kansas City, MO 64108
816-374-3307
U.S. EPA, Region 8
Solid Waste Section
1860 Lincoln St.
Denver, CO 80295
303-837-2221

U.S. EPA, Region 9
Solid Waste Program
215 Fremont St.
San Francisco, CA 94105
415-556-4606

U.S. EPA, Region 10
Solid Waste Program
1200 6th Ave.
Seattle, WA 98101
206-442-1260
                                                   U.S.  Envir-r.-v.T
                                                   Ecflr.r  r,
                                                   Y.'O o.  _..•
                                                      ition'-Agency-

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