SEPA
            United States
            Environmental Protection
            Agency
            Municipal Environmental Research
            Laboratory
            Cincinnati OH 45268
EPA-600/2-78-057
June 1978
            Research and Development
A Study of
Forced Aeration
Composting of
Wastewater Sludges

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                RESEARCH REPORTING SERIES

Research reports of the Office of Research and Development. US Environmental
Protection Agency, have been grouped into nine series These nine broad cate-
gories were established to facilitate further development and application of en-
vironmental technology Elimination of traditional grouping was consciously
planned to foster technology transfer and a maximum interface in related fields.
The nine series are:

      1   Environmental Health  Effects Research
      2   Environmental Protection Technology
      3   Ecological Research
      4   Environmental Monitoring
      5.  Socioeconomic Environmental Studies
      6   Scientific and Technical Assessment Reports (STAR)
      7   Interagency Energy-Environment Research and Development
      8   "Special" Reports
      9   Miscellaneous Reports

This report has been assigned  to the ENVIRONMENTAL PROTECTION TECH-
NOLOGY series This series describes research performed to develop and dem-
onstrate instrumentation, equipment,  and methodology to repair or prevent en-
vironmental degradation from point and non-point sources of pollution. This work
provides the new or improved technology required for the control and treatment
of pollution sources to meet environmental quality standards
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia  22161

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                                     EPA-600/2-78-057
                                     June 1978
                A STUDY OF
        FORCED AERATION COMPOSTING
           OF HASTEHATER SLUDGE
                    by
            William F.  Ettlich
               Anne E.  Lewis
             Culp/Hesner/Culp
          Clean Water Consultants
    El Dorado Hills, California  95630
          Contract No. 68-03-2186
              Project Officer
           Francis L. Evans, III
               Task Officer
               Gerald Stern
       Hastewater Research Division
Municipal Environmental Research Laboratory
          Cincinnati, Ohio  45268
MUNICIPAL ENVIRONMENTAL RESEARCH LABORATORY
    OFFICE OF RESEARCH AND DEVELOPMENT
   U.S. ENVIRONMENTAL PROTECTION AGENCY
          CINCINNATI, OHIO  45268

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                              DISCLAIMER
     This report has been reviewed by the Municipal Environmental Research
Laboratory, U.S. Environmental Protection Agency, and approved for publi-
cation.  Approval does not signify that the contents necessarily reflect
the views and policies of the U.S.' Environmental Protection Agency, nor
does mention of trade names or commercial products constitute endorsement
or recommendation for use.
                                    ii

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                                 FOREWORD
     The Environmental Protection Agency was created because of increasing
public and government concern about the dangers of pollution to the health
and welfare of the American people.  Noxious air, foul water, and spoiled
land are tragic testimony to the deterioration of our natural environment.
The complexity of that environment and the interplay between its components
require a concentrated and integrated attack on the problem.

     Research and development is that necessary first step in problem solu-
tion, and it involves defining the problem, measuring its impact, and search-
ing for solutions.  The Municipal Environmental Research Laboratory develops
new and improved technology and systems for the prevention, treatment, and
management of wastewater and solid and hazardous waste pollutant discharges
from municipal and community sources, for the preservation and treatment of
public drinking water supplies, and to minimize the adverse economic, social,
health, and aesthetic effects of pollution.  This publication is one of the
products of that research; a most vital communications link between the
researcher and the user community.

     Wastewater sludge can be converted by composting into a soil condition-
er as one method of recycling resources.  Wastewater sludge has been com-
posted on a regular schedule at Beltsville, Maryland, and Bangor, Maine,
using forced aeration technology developed by the U.S. Department of Agri-
culture, Agricultural Research Service, Beltsville, Maryland.  Both of these
operations have received grant funds from the U.S. Environmental Protection
Agency.

     The results of an intensive study of these two operations are presented
in this report.
                                      Francis T. Mayo, Director
                                      Municipal Environmental Research
                                      Laboratory
                                     iii

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                                 ABSTRACT
     This study was initiated with the overall objective of developing an
independent assessment of the forced aeration wastewater sludge composting
method as practiced at Beltsville, Maryland, and Bangor, Maine.  A number of
visits were made to both sites to observe operations under all weather con-
ditions and to gather data.  The analysis developed herein is based on in-
formation obtained during the site visits, information provided by various
agencies and individuals, and independent observations and calculations.

     Results of the study indicate that forced aeration wastewater sludge
composting can be carried out in a satisfactory manner under nearly all
weather conditions, including severe New England winters.  A number of prob-
lems and potential problems are identified along with possible solutions.
Costs per unit of sludge processed are very dependent on the size of the
operation and the methods used.  Several possibilities are explored for re-
ducing costs by modifying operations.

     This report was submitted in partial fulfillment of Contract No.
68-03-2186 by Gulp/Wesner/Culp - Clean Water Consultants under the sponsor-
ship of the U.S. Environmental Protection Agency.  This report covers the
period June 1, 1976 to July 1, 1977, and work was completed as of July 1,
1977.
                                     iv

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                                CONTENTS

Foreword	ill
Abstract	iv
Figures	vi
Tables	vii
Acknowledgments	viii

   1.   Introduction 	   1
   2.   Conclusions and Recommendations	   2
   3.   Operations	   4
             General description 	   4
             Site visits	   5
             Materials handling aspects	   5
             Monitoring	  16
             Site considerations	  20
             Weather	20
             Nuisances	25
   4.   Considerations for Future Operations 	  26
   5.   Compost Distribution	29
   6.   Costs	31
   7.   Pathogens	34
   8.   Results and Discussion	43

References	47
List of Metric Conversions . .	49
Appendix:  Forced aeration composting and applications  	  50

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                                 FIGURES

Number                                                                Pa9e

   1    Beltsville composting site layout	7

   2    Bangor composting site layout	 . 13

   3    Total coliform densities 	 36

   4    Fecal coliform densities 	  	 37

   5    Salmonella densities 	 38

   6    Relationship between disease risk and salmonella,
          coliforms, and fecal coliforms 	 42
                                    vi

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                                 TABLES

Number                                                                pa

   1    Site Visits and Weather ...................    6

   2    Beltsville Equipment .... ...... ..........   10

   3    Beltsville Materials Requirements For 15,000 Wet
          Ton Annual Sludge Input ..................   H
   4    Approximate Materials Output, Beltsville Type
          Operation. . .
   5    Estimated Annual Operations Requirements, Bangor ......  17

   6    Bangor Equipment ......................  18

   7    Bangor Materials Requirements For 2,170 Wet
          Ton Annual Sludge Input ..... .............  18

   8    Approximate Materials Output, Bangor Type
          Operation .........................  19

   9    Beltsville Actual and Projected Costs .........  ...  32

   10    Bangor Composting Costs , 1975-1976 .............  33

   11    Sources  of Pathogen Data ...............  •  •  •  35

   12    Summary  of Bacteria Data ..................  35

   13    Relation of  Dosage of Salmonella  typhi to  Disease.  .....  40

   14    Dose of  Various Species and Strains  of Salmonella That
           Caused Disease in Human  Volunteers ............  41
                                    vii

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                               ACKNOWLEDGMENTS

     Culp/Wesner/Culp - Clean Water Consultants gratefully acknowledge the
cooperation of many agencies in providing information and data for this re-
port.

     The Maryland Environmental Service and United States Department of
Agriculture, Agricultural Research Service, provided data related to the
Beltsville operation and unlimited access to the site.  The cities of Bangor,
Maine, and Durham, New Hampshire,provided complete data related to their
operations in addition to site visits.

     The personnel of the Ultimate Disposal Section, Wastewater Research
Division, US EPA, MERL, provided much of the coordination required between
agencies and performed the technical review of the final report.
                                    viii

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                                'SECTION 1

                              •INTRODUCTION
     The objective of this study is to report on the major operational
'aspects of the forced-aeration wastewater sludge composting method as prac-
ticed at Beltsville, Maryland  (Beltsville), and Bangor, Maine  (Bangor).
Beltsville has been supported from December, 1975, through December, 1977,
as follows:

     Blue Plains Participants
     EPA Region III
     U. S. Dept. of Agriculture
     EPA Office of Research and
        Deveopment
                      Total

     Bangor has received  grant funding from the EPA  Office of  Solid  Waste
Management Programs.  The forced-aeration composting process is a develop-
ment of the Agricultural  Research Staff  at  Beltsville,  Maryland.

     The principal  sources of  information and  data were the actual opera-
tions  at Beltsville and Bangor with  some support  information  from the
operation at  Durham, New  Hampshire,  and  the windrow  composting operation at
the  County Sanitation Districts  of Los Angeles County  Joint Wastewater
Treatment Plant at  Carson, California.

     This report  represents  an independent  assessment of the  forced-aeration
technique for composting  raw wastewater  sludge based on evaluation of avail-
able data and on-site observations.

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                                SECTION 2

                     CONCLUSIONS AND RECOMMENDATIONS
 CONCLUSIONS

     The forced aeration method of wastewater sludge composting is a bio-
 logical stabilization process, but in terms of actual work is basically a
 materials handling operation.  All operations to date use mobile equipment
 with little demonstration of fixed materials handling equipment.  The use
 of mobile equipment does provide for flexible and satisfactory materials
 handling, but use of fixed equipment might contribute to decreased opera-
 tional costs for some parts of the operation.  Presently, operation and
 maintenance costs vary from $86 to $150 per dry ton of wastewater solids
 processed and depend on the installation size.  Removal of costs related to
 research and optimization of operations would reduce sludge composting costs
 to $50 to $80 per dry ton of wastewater solids.

     Composting has been accomplished outdoors in all types of weather on a
 continuous basis at both Beltsville and Bangor.  Heavy rain and extreme cold
 have been minor problems and require more careful operation, but have not
 interrupted composting operations.

     Screening is greatly affected by weather.  Screening cannot be accom-
 plished outdoors in rainy or very cold weather.  Therefore, screening must
 be accomplished during favorable weather or the operation must be weather
 proofed.  Screening can be a limiting factor for a composting operation and
 careful consideration must be given to the type of equipment, the average
 daily screening capacity, the amount of material to be screened, moisture
 content of the material to be screened, and the number of days during which
 screening can take place.

     Careful consideration must be given to the type and availability of
 bulking agent to be used.  Bulking agents can be a major operational cost
 and may be difficult to obtain in certain areas of the country.  There are
 several potential techniques for conservation and reuse of bulking agent.
 The most promising is to use compost from a pile being torn down as bulking
 agent for new sludge.

     The operations at Beltsville and Bangor are carried out with minimal
nuisances.  Some odors are generated at both sites, but public complaints
have been nil and operations are never shut down; in fact, it is impossible
to "shut down" operations because composting and curing are continuous pro-
cesses.   Operations can be stopped by hauling the materials to a landfill
or disposal site.

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     Waterproofing of some of the normal unit operations is desirable.   Com-
posting has been carried out at Beltsville for several years on an outdoor
gravel base.  The recent installation of hard surfacing at Beltsville has
improved the operations and should be considered for all new installations.
The installation of covered areas for mixing, curing, and screening should
be considered for areas with heavy and prolonged rainfall.

     Sufficient pathogen and indicator organisms data are available to
develop some generalized conclusions.  Based on these data and additional
calculations, the risk of disease outbreak in adult humans from properly
operated wastewater sludge composting appear to be very slight considering
the tolerance level to pathogens exhibited by adult humans.  Some risk may
exist, however, because there is no way to assure complete kill of all
pathogenic or parasitic organisms in outdoor composting unless the compost
is sterilized.  Generally, the use of wastewater sludge based compost will
be subject to regulatory agency requirements in most  states.

RECOMMENDATIONS

      Operational methods  should be investigated to minimize materials hand-
ling,  use  of bulking  agent,  and  screening.   Several  methods which offer
potential  savings  in  these  operations  are suggested  herein.  One  major
method is  reuse of unscreened compost  as  bulking agent through one or more
cycles.  Some of these  methods have  been  tested on a limited scale,  but
should be  tested and  refined further.   Use of these  methods should reduce
operation  costs  and also  provide some  operation benefits such  as  conserva-
tion of heat during cold  weather operations.

      Careful plans should be developed for marketing or disposing of the
 compost product.   Some revenue may be realized from selling the compost, but
 the return will not cover the total  costs of producing the compost.  Methods
 are discussed for reducing compost production if desired, or necessary,
 because of disposal limitations.

      It is difficult to make recommendations related to pathogenic organisms
 because any conclusions or illustrations developed herein are only opinions.
 Some pathogenic organisms will likely be present in the compost unless it
 is completely sterilized.  Even with sterilization, reinfestation by certain
 pathogenic bacteria is possible.  The possibility of disease outbreak re-
 lated to the use of properly developed wastewater sludge compost is very
 small because humans do exhibit a tolerance to fairly high levels of patho-
 genic organism infection before actually exhibiting  signs of the disease.
 It is recommended that composting operations be carried out to assure  inter-
 ior pile temperatures greater than 60°C  for several  days and that a 30  day
 curing period be utilized  following composting.  These  steps will assure
 the highest possible pathogen kill.  Other  steps to minimize  the ingestion
 of compost  by humans such  as use of compost on non  food  crop  applications
 will reduce any potential of disease outbreak.

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                                 SECTION 3

                                 OPERATIONS
 GENERAL DESCRIPTION

      The Beltsville composting site has been used for several years for the
 research and demonstration project.  The composting operations are  carried
 out by Maryland Environmental Service (MES)  personnel.   The research acti-
 vities are carried out by the U.S.  Department of Agriculture, Agriculture
 Research Service (ARS).   Even though research activities are being  carried
 out at Beltsville,  the basic  sludge composting operations are similar to
 what may be carried out by any municipality.   In 1976,  a total of 14,459
 wet tons of undigested wastewater sludge conditioned with lime and  ferric
 sulfate and dewatered  (approximately 23% solids)  from the Washington,  D. C.
 Blue Plains plant was  composted at  Beltsville using the extended pile  forced-
 aeration method.   This method is described in Appendix  A.   Operations  were
 carried out on  a regular schedule as would be required  by a municipal  sludge
 processing facility.   In the  first  part of 1976,  sludge deliveries  were made
 7 days a week while, during the last part of  1976,  deliveries were  made 5
 days a week with only partial staffing  on weekends.   Sludge deliveries
 averaged approximately 300  wet tons per week  (approximately 60 wet  tons per
 day on a 5 day  per  week  basis).  Sludge delivery was accepted every working
 day except when Blue Plains could not provide sludge or the delivery trucks
 could not operate.  This delivery schedule represents operation typical for
 a municipality  serving the  equivalent of 140,000  to 160,000 persons.   Sludge
 deliveries have been as  high  as 100 wet tons  per  day for several days  at a
 time at Beltsville.

      The  analysis of operations at  Beltsville provides  guidance for planning
 a regular municipal wastewater sludge composting  facility.  This report will
 focus on  the regular operations at  Beltsville and will  not  emphasize the
 research  operations except where specific data such  as pathogen organisms
 densities provide applicable  information.  ^Sh& Beltsville operations
provide useful  information  for municipal sludge  composting during various
 weather conditions  including  cold,  snow, rain,  inversion conditions, and
 fair weather.

      Forced-aeration wastewater sludge  composting also has been carried out
 by  the municipality of Bangor for over  two years, through two winters, out-
 doors and in very  severe weather conditions.   In 1976,  the City composted
 approximately 1,944 cu yd (332 dry  tons) of  23 percent solids, dewatered
 raw (primary)  sludge at the City owned  site  at the Bangor International
 Airport.  Total Bangor sludge production in  1976 was 3,033 cu yd  (525 dry

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tons).  The sludge not composted (1089 cu yd)  was hauled to a landfill.

     This report is based on observations of the Beltsville and Bangor muni-
cipal sludge composting operations with data input from several on-site
visits and information provided by MES, ARS, the Town of Bangor, and USEPA.

SITE VISITS

     To develop an independent and realistic assessment of the Beltsville
and Bangor operations/ considerable on-site observations were made at both
sites under various weather conditions as shown in Table 1.  Information
was also obtained from discussions with operating, supervisory, and admin-
istrative personnel.  Cooperation of all operating agency personnel was
outstanding.

MATERIALS HANDLING ASPECTS

     Optimization of materials handling is of primary importance for suc-
cessful municipal sludge forced air composting operations.  The volume of
materials handled varies almost directly with the input sludge quantity.
The type and characteristics of materials handled varies from site to site
depending on type of sludge, type of bulking agent, and weather conditions.
The optimum or most cost effective materials handling methods will vary
significantly depending on the size and how the operation is carried out.
Beltsville and Bangor provide information primarily on the use of mobile
equipment for materials handling because neither operation was using fixed
equipment at the time of this study.

Beltsville

     An approximate scale layout of the Beltsville operations site is shown
in Figure 1.

     Undigested sludge cake  (approximately 23 percent solids) from the
Washington, D. C. Blue Plains wastewater treatment plant is delivered to
Beltsville in 10 wet ton loads by conventional  3 axle dump trucks.  Two
trucks are used.  Each truck makes 3 trips for  60 wet ton per day delivery.
Delivery generally begins early in the morning  and continues into early
afternoon.  Prior to the sludge delivery, pads  of bulking agent are prepared
in the mixing area.  These pads are 9 to 10 feet wide, 1 to 2  ft deep and
as long as required for the bulking agent to sludge ratio mix  for one truck-
load of sludge.  The sludge trucks arrive on site, are weighed, and then
dump the sludge onto the bulking agent pad.  A  front loader is  used to
spread the sludge evenly over the top of the bulking agent.  The Terex
composter then moves along one side of the sludge - bulking agent pad and
then along the other side, mixing the materials toward the middle to  form a
partially mixed windrow of triangular  cross section.  The  Roto-Shredder then
passes through the windrow, turns around, and passes back  through the win-
drow.  This operation mixes the sludge and bulking agent to  form a  relative-
ly homogeneous mixture.  The Terex composter and  Roto-Shredder are  both used
because they are available at Beltsville.   Satisfactory mixing can  be
accomplished using  either machine alone.  Mixing  can also  be accomplished

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                   TABLE 1.  SITE VISITS AND WEATHER
Site
Beltsville
Beltsville
Beltsville
Beltsville
Bangor
Bangor
Date
9-27-76
9-28-76
9-29-76
1-26-77
1-27-77
1-28-77
4-4-77
4-5-77
4-6-77
4-7-77
6-21-77
6-22-77
9-22-76
9-23-76
2-23-77
2-24-77
2-25-77
Weather
Fair
Fair
Fair
Cold, Snow on ground,
some inversion , no
wind in early mornings
Heavy rain, windy
Rain f
Fair, windy
Cloudy, windy
Fair
Fair
Fair
Fair
Fair
Cloudy
Freezing rain, snow
Range of
temperature, °G
10 to 15
10 to 15
-9 to 2
-9 to 4
-9 to 7
4 to 13
4 to 13
2 to 13
1 to 13
21 to 27
21 to 27
2 to 18
2 to 18
-9 to -1
-9 to -2
-4 to -1
Bangor
6-1-77
                                           Clear
21 to 27

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SITE
ENTRANCE
           SCREENED
           COMPOST
           STORAGE
COVERED
MAINTEN-
ANCE
SHOP
                                                                      lULKING
                                                                    AGENT
                                                                   STORAGE
                  ADMINISTRA
                  TION AND
                                                    APPROXIMATE SCALE
                                                       1"  = 200'
              Figure  1.   Beltsville  composting site layout.

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 using only the front loader, but is more time consuming to produce a good
 mix.  It is felt that a good mixture, free of large sludge balls, is impor-
 tant for good composting and producing a high quality product.

      Beltsville has been using the extended forced-aeration pile composting
 configuration.  Material is added to the pile each day and aeration pipes
 are spaced about every 8 feet on center.  The composting pad for each days
 sludge-bulking agent mixture is prepared by laying out the aeration piping
 on the asphalt composting pad and covering this pipe with a 12 in. layer of
 wood chips using a front loader.  The sludge-bulking agent mixture is then
 placed on the wood chip base using a front loader.  The mixture is piled to
 a height of about 8 ft.  The top and ends of the pile are then capped with
 an 18 in. layer of unscreened compost or a 12 in. layer of screened compost.
 At the end of each days operation the side of the pile (which will be added
 to the next day)  is covered with a thin layer of compost.  The blower is
 connected to the piping and a 5 cu yd pile of screened compost is placed
 over the end of the blower discharge piping for deodorizing the discharged
 air.   The blower pulls air from the composting pile and discharges to the
 deodorizing pile.   The blower is generally operated on an on-off cycle con-
 trolled by a timer.  The duration of the on and off cycles is adjusted to
 suit the particular operating conditions.

      Generally,  compost is removed from the opposite end of the extended
 pile each day or every other day after 21  days of composting.   This part of
 the pile is torn down using a front loader and is moved to the curing pile.
 At Beltsville,  the  aeration pipe is a light weight plastic considered ex-
 pendable and therefore,  is moved with the  compost.   The compost stays in
 the curing pile  for at least 30 days,  usually for a much longer period,
 awaiting screening  or off-site use.   The unscreened compost can be stored
 for long periods  depending on the needs of the particular operation and
 the screening and compost distribution operations.

      Processing  of  the dewatered raw sludge cake and formation of the com-
 post  pile must be carried out on a regular basis consistent with raw sludge
 delivery.   Raw sludge is  mixed with bulking agent and processed into a
 compost  pile promptly as  it is received on site to avoid odors and health
 hazards.   Raw sludge is not stored on site.   Should site conditions or
 weather  shut down operations (there are practically no instances of this
 occurring at Beltsville)  sludge would not  be delivered but instead be
 either stored  at  the Blue Plains plant or  diverted to other disposal sites.

      Screening is used to separate  the wood chips  from the compost:  (1)  so
 that a portion  of  the chips  can be reused,  (2)  to control  the maximum parti-
 cle size  of the compost,  and  (3)  to improve the carbon-nitrogen ratio of
 the finished compost.  Most screening  is performed using  a 5/8-inch mesh
 rotary drum screen.   The  drum is 7  feet in diameter and about  14 feet long.
 The tilt  of the drum is adjustable  as  is the feed  rate.   Screening can be
 scheduled  independent of  other operations  because  of unscreened compost
 storage availability.  In practice,  however,  enough compost is  screened  to
meet:  (1)  any on-site needs,  (2)  the  demand from users,  and  (3)  to  provide
room in the unscreened storage  area  for  current production.  At Beltsville,
compost is  screened  at all  times when  the  temperature  is  above  freezing  and


                                      8

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rain is not falling.  Peak hourly capability of the drum screen with fairly
dry material is about 50 cu yd.  However, under actual conditions of start-
up, shutdown, cleanup, and typical breakdowns, the input drum screen capa-
bility is about 150 to 250 cu yd per day.  The screen is mounted on wheels
and can be moved with the front loader for cleanup.  Moving the drum screen
permits use of the front loader for cleanup rather than having to clean by
hand.

     Other site operations include regular cleanup of work areas, receipt
and storage of bulking agent, loading and measurement of finished compost
for users, and equipment maintenance.

     The staff at Beltsville consists of 8 people; 2 administrative and 6
operating.  This number is more than actually needed for normal operations.
The additional personnel are used for special operations and to support
the research demonstration program.  The operating staff is highly trained,
each member is qualified on each piece of equipment, and the staff is able
to perform all preventative maintenance and much of the repair work.  Per-
sonnel and equipment are available for the composting operation full time.
A list of equipment is shown in Table 2.

     The approximate materials quantities used in the Beltsville operation
are shown in Table 3.  These quantities are based on an annual undigested
sludge cake  (approximately 23 percent solids) input of 15,000 wet tons, a
ratio of two and one half parts wood chip bulking agent to one part sludge
cake by volume, and 5/8-inch screening of all compost for a wood chip recov-
ery and recycle of 70 percent.  Output or production quantities are shown
for both a 12 in  screened compost pile cover and an 18 in  unscreened com-
post pile cover in Table 4.  The unscreened compost production is based on
15 percent reduction in sludge volume during composting and curing.  This
example serves only to illustrate general concepts because the materials
loss through composting and curing are estimated and have not been precisely
documented at existing operations.

Bangor

     A typical operations layout of the Bangor site is shown in Figure 2.
The layout is to approximate scale.

     Undigested raw lime conditioned sludge cake  (approximately 25 percent
solids) is delivered from the City of Bangor primary wastewater treatment
plant in 5 to 7 cu yd containers by a single lift and carry type truck.
The sludge is delivered to the composting site located at the Bangor Inter-
national Airport approximately 3 miles from the treatment plant.  Generally,
the raw sludge is dewatered, delivered, and composted once a week; on
occasions twice a week,  usually the dewatering operation is started the day
before so that all available sludge containers are  filled the morning com-
posting is to commence.  Sludge hauling to the site begins early on the
morning of composting.  An operator and 4 cu yd front loader is available
early at the site on the day of composting.  As the containers of sludge
are delivered to the site they are dumped on a previously prepared bed of
bulking agent in the mixing area, mixed immediately with the front loader,

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      TABLE 2.  BELTSVILLE EQUIPMENT
2 Terex Rubber Tired Front Loaders, 4.5 cu yd
2 Dump Trucks, 10 Ton, 3 Axle
2 Flat Bed Trucks, 1.5 ton
2 Pickups
2 Rubber Tired Farm Tractors, one with loader
1 Rotary Screen with power unit
1 Sweco Screen, fixed  (new)
1 Mobile Rotary screen, small (not used)
1 Terex Composter
1 Imco Roto-Shreader
1 Large conveyor with engine drive (not used)
1 Fixed Toledo Truck Scale
1 Mobile Office
1 Storage Building
1 Lot small equipment and hand tools
                    10

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              TABLE 3.  BELTSVILLE MATERIALS REQUIREMENT FOR
                        15,000 WET TON ANNUAL SLUDGE INPUT
Limed raw sludge, wet tons                         15,000
     Solids, percent                                   23
     cu yd                                         20,700
     Density, Lb/cu yd                              1,450
     dry tons                                       3,450

Extended pile construction
     Sludge, cu yd                                 20,700
     Bulking agent
          mixing w/sludge, cu yd                   51,750
          pile base, cu yd                          8,100
     Pile cover
          screened compost, cu yd                  12,000 (12 in.cover)
          unscreened compost, cu yd                18,000 (18 in.cover)

Individual pile construction
     Sludge, cu yd                                 20,700
     Bulking agent
          mixing w/sludge, cu yd                   51,750
          pile base, cu yd                         17,000
     Pile cover
          screened compost, cu yd                  24,000 (12 in.cover)
          unscreened compost, cu yd                36,000 (18 in. cover)
                                    11

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              TABLE 4.   APPROXIMATE MATERIALS OUTPUT, BELTSVILLE TYPE OPERATION
**
Case
Extended pile with:
screened compost cover
unscreened compost cover
Net
unscreened
compost
production,
cu yd
82,260
87,660
Net
screened
compost ^
production,
cu yd
39,170
35,210
Bulking agent, cu
Total
required Recycled
59,850 43,100
59,850 52,450
yd
*
Net used
(new make-up)
16,750
7,400
Individual piles with:
screened compost cover
unscreened compost cover

101,070 51,570
111,355 43,351

68,750
68,750

49,500
68,000

19,250
750
 *   Does not reflect actual Beltsville operations because only a portion of the Beltsville
     compost  is  screened.

 **  Materials input shown in Table 3.
Assumptions:
     1.   15 percent reduction in sludge volume during composting and curing.
     2.   10 percent of the bulking agent lost in composting and curing cycle.
     3.   20 percent of the bulking agent lost in screening (passing through screen into finished
          compost).
     4.   15,000  wet  ton  annual  sludge  input.

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                BULKING
                AGENT
                STORAGE
      COMPOSTING
        PILE
    (4 or 5 PILES)
     SCREENED
      COMPOST
MIX-
ING
AREA
         PAVED AREA
                                    UNSCREENED
                                    'COMPOST
                                     STORAGE
                                   • SCREENING
                             APPROXIMATE SCALE
                                 1"  =  200'
Figure 2.  Bangor composting site layout.
                      13

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 and the compost pile is formed over a previously prepared base.   Generally,
 one composting pile is constructed per week and typically consists of
 approximately 40 to 60 cu yd of raw digested sludge cake mixed in 1:3 ratio
 with about 120 to 180 cu yd of bulking agent.  Approximately 6 to 8 trips
 must be made to the site to deliver the sludge cake.   The mixing and pile
 construction requires a 10 hour day.  Materials are measured by counting
 loader bucket loads.

      Bark is currently used as a bulking agent.  Most composting piles are
 mixed in a 3:1 ratio of bulking agent to sludge cake.   The bark consists of
 a wide range of particle sizes from very fine to fireplace size  logs.   When
 the bark moisture content is less than 50 percent it is satisfactory for
 composting.   Moisture is a problem during rainy weather because  the bark is
 stored outside.   During winter,  there is little rain and the bark is quite
 satisfactory.   A more uniform sized bulking agent,  similar to chips, would
 probably help the composting operation.

      The base for the compost pile is prepared using 7 ft lengths of per-
 forated schedule 40 steel pipe joined  together by short pieces  of plastic
 pipe.   The City found that the short lengths of steel  pipe can be removed
 from the pile without significant damage and reused many times.   Longer
 pipes were used previously,  but  were easily bent when  pulled from the  pile.
 The City has been experimenting  with many different pile configurations.
 Currently, no base material  is used;  the sludge-bulking agent mixture  is
 placed directly on the pad and aeration  pipes.   The City has also satisfac-
 torily used  unscreened compost as the bulking agent in a number  of piles.
 Unscreened compost has been  used up to three cycles as bulking agent with
 good results and thereby dramatically reduced requirements for new bulking
 material.  The City plans further tests  using unscreened compost as bulking
 agent.   The  reuse of  unscreened  compost  may increase the nutrient content
 of  the finished  product;  however,  this needs to be  confirmed.

      The  compost piles are constructed as high as the  front loader can
 reach and capped with 1 to 2  ft  of unscreened compost.   The finished pile
 is  10  to  12  ft high.   The  blower is then hooked up  and generally operated
 on  an  on-off cycle  drawing air from the  pile.   During  cold weather,  the
 warm exhaust air from an older composting pile  is piped into a new pile  for
 a few  days to  rapidly increase the temperature  of the  new compost pile.
 The  exhaust  air  from  an older composting pile is  very  wet and will cause
 high moisture  levels  in the new pile  receiving  the  air if used more than
 the  first several days.  The  City has  also purchased a ram air heater  to
 provide initial  heat  to the piles.

     The City  found that during  cold weather  all  available  heat must be
 conserved to help the piles come  up to temperature.  Reuse  of unscreened
 compost provides  a warm bulking  agent.   The  interiors  of  the  bark storage
piles are also sources  of warm materials  for  mixing.   Generally,  if the
 sludge-bulking agent mixture  can  be kept  about  4°C  the pile will  perform
much better  than  if the  mixture  falls below  4°C.  Recycle of  warm exhaust
 air from an older composting pile  into the new pile is also helpful for the
 first few days.
                                     14

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     The piles are composted at least 21 days.  Temperature and oxygen
levels are monitored every 2 to 5 days during the composting cycle.  The
blower operating cycle is adjusted according to the performance of the
pile.  The aeration pipes, blowers, and moisture traps are checked for
freezing during cold weather because of the large amount of moisture drawn
through the aeration piping.

     At the end of the composting cycle the pile is torn down, usually at
the time another pile is constructed.  The material removed from the pile
is either used as the bulking agent for the new pile or is transferred to
curing.  As the pile is torn down the 7 ft lengths of aeration pipe are
salvaged, cleaned out, and piled to the side for reuse.

     Raw sludge is not stored at the compost site, but is stored at the
plant.  Generally, operations are scheduled so that sludge is dewatered
and a compost pile constructed once a week.  The exact day of pile construc-
tion is varied depending on weather conditions.  The City has been able to
compost nearly all of the sludge production simply by picking a good day
each week for compost pile construction.  During 1976, about 1,000 cu yd
(700 wet tons) of dewatered sludge was hauled to landfill rather than com-
posted, becAjise composting at the time was being done by public works
personnel, not treatment plant personnel.  At times, public works personnel
were unavailable to compost the sludge.  Treatment plant personnel feel
that they will seldom have to haul sludge to landfill.  Liquid sludge is
stored in the thickeners until dewatered.  However, some additional liquid
sludge storage capability would be helpful because of the cyclic nature of
the dewatering operations.  The plant is able to operate by storing sludge
in the thickeners.

     The City uses a Lindig rotary drum screen to screen compost prior to
distribution.  The drum is presently fitted with a 1-in. mesh screen.  City
personnel are planning to construct a 5/8-in. screen assembly so that either
size material can be produced.  Tests performed by the City indicate that
the screen is capable of handling about 20 to 25 cu yd  (900 Ib per cu yd)
of feed per hour under the best conditions.  The screen is fed with a front
loader.  One loader operator and a laborer are required during operation.
The City performed screening during late summer and fall of 1976, but has
not been able to screen during winter 1976-77.  Most of the unscreened com-
post production is stored in curing piles and about 3,000 cu yd is now on
hand awaiting screening.  It is estimated that the screen can process about
100 to 150 cu yd of feed per day based on typical operations and that 20 to
30 days of screening will be required to process the present 3,000 cu yd
stock.

     Currently, operations at Bangor are being carried out by treatment
plant personnel under the direction of the treatment plant superintendent.
There are no full time composting personnel because of the cyclical nature
of the operations.  Approximately 11 man-hours per week are required at
the site, primarily for loader operation.  In addition, approximately 9
man-hours per week are required for a truck driver to deliver sludge to the
site.  Sampling and monitoring for temperature and oxygen content requires
10 hours per week not including the pathogen and heavy metals monitoring

                                      15

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 which is performed under contract by the University of Maine.   The super-
 vision and administration requirements are about 15 man-hours  per week.
 Annual equipment and labor requirements are shown in Table 5.

      The equipment used for composting operations is shown in  Table 6.
 This equipment is provided by the City motor pool and is available "for  com-
 posting when needed.

      The approximate materials quantities based on 1976 sludge volume for
 the Bangor operation are shown in Table 7.  These quantities are based  on
 an annual sludge input of 2,170 wet tons and a mixture of 3 parts bulking
 agent to one part sludge.  The calculated materials production is shown in
 Table 8 for three assumed cases.  These production outputs assume a 15
 percent reduction in sludge volume during composting and curing and one
 inch screening of compost before distribution.  Recovery of bark is esti-
 mated at 70 percent by either screening an/or recycle of the unscreened
 compost as bulking agent.  Table 8 serves only to provide an approximate
 indication of materials quantities.

 MONITORING

      Regular monitoring of operations  can provide a good indication of  com-
 posting effectiveness.   The regular operations (not the research operations)
 at Beltsville are so routine and dependable that piles are monitored only
 occasionally.

      The piles at Bangor are monitored regularly for interior  temperatures
 and oxygen levels.   Generally,  this  monitoring is performed every 2 to  5
 days at several points  in each pile.   These data are used to judge the pile
 performance and to set  the blower operating cycle.   At the end of the com-
 posting period each pile is sampled  and tested for moisture content and
 pathogens.   In addition,  random sampling and pathogen testing  is performed
 on raw sludge,  curing,  and finished  compost.   Some heavy metals and nutri-
 ent testing is also performed.

      Experiences at Durham and Bangor  tend to indicate that regular moni-
 toring of pile temperature can provide a direct indication of  pile compost-
 ing performance and can help to pinpoint problems.   For instance,  the
 initial rate of temperature increase is a good indicator of the composting
 efficiency to be expected.   Generally,  the temperature of a poorly con-
 structed pile (too wet  or not well mixed)  will rise slowly and in many
 cases  will  not reach proper temperatures.   At Durham,  such piles have been
 torn down and rebuilt with vastly improved performance the second time.
 Durham also found it desirable  to reverse air flow part way through the
 composting  process  and  the time of reversal was determined from temperature
 monitoring.

     Additional  regular monitoring can be performed  to include  oxygen levels
within the pile, pathogens, heavy metals  and  nutrients.   For a  small oper-
 ation, at least  regular  temperature  monitoring should be performed.   It
 has  been  found useful to  plot the composting temperatures on a  regular
 basis  (daily during the  first few days as the pile  comes up to  temperature)


                                     16

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       TABLE 5.  ESTIMATED ANNUAL OPERATIONS REQUIREMENTS, BANGOR

                                   Labor,             Equipment,
Operation 	hours	hours
Composting, labor                   572
            front loader                                  468

Sludge hauling, labor               468
                truck                                     468

Monitoring, labor                   520
            pickup                                        520

Administration, labor               780

Screening  (8,000 cu yd), labor    1,040
                 screen                                   520
                 front loader                             520

Maintenance, labor                  100
This Table is based on information provided by the City of Bangor
personnel.
                                    17

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              TABLE 6.  BANGOR EQUIPMENT
      1 Case W24B Rubber Tired Front Loader, 4 cu yd
      1 Rubber Tired Front Loader, 1.5 cu yd
      1 Truck, Sludge container hauling
      1 Mobile screen, Lindig
        Small tools as required
        Miscellaneous vehicles as needed from motor pool
    TABLE  7.  BANGOR MATERIALS REQUIREMENTS FOR
              2,170 WET  TON ANNUAL  SLUDGE  INPUT
Limed raw sludge, wet tons           2,170
            solids, percent          23
            cu yd                    3,000
            Density,  Ib/cu yd        1,450
            dry  tons                  500

Static pile construction
            sludge, cu yd            3,000
            bulking agent, cu yd     9,000
            pile cover, cu yd        1,560
                          18

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           TABLE  8.  APPROXIMATE MATERIALS OUTPUT, BANGOR TYPE OPERATION.
Case*
Net
unscreened
compost
production,
cu yd
Net
screened
compost
production ,
cu yd

Total
regjd
Bulking agent,
Recycled
cu yd
Net used
(new make-up)
New or recycled
   bulking agent
   used in pile
   construction          10,920

Unscreened compost
   from pile used
   as bulking agent
   for one cycle          6,240

Unscreened compost
   from pile used
   as bulking agent
   for two cycles         4,654
4,160
3,198
2,785
9,360
4,680
3,114
6,760
3,042
1,868
2,600
1,638
1,246
*  Materials input shown in Table 7.

Assumptions;
     1.   15 percent reduction in sludge volume during composting and curing.
     2.   10 percent of the bulking agent lost in each composting and curing cycle.
     3.   20 percent of the bulking agent lost in screening (passing through screen  into
          finished compost).
     4.   2,170 wet ton annual sludge input.

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 during the composting period along with daily precipitation and  air  temper-
 ature.   This  information provides a profile  of  each  pile.   It may  also be
 desirable to  monitor a temperature near the  outside  of  the  pile  as a check
 on minimum temperatures and the  effectiveness of the pile cover.

      Bangor and Durham have been able  to provide pathogen monitoring through
 a cooperative agreement with a local university.

 SITE  CONSIDERATIONS

      The site location should be selected with  great care considering trans-
 portation/  adjacent  land use, drainage,  winds and similar factors.   It is
 desirable to  provide a buffer strip around the  site, preferably  one that
 will  also block the  view.   Slight odors are  generated at times and,  al-
 though  practically no complaints are received at operating  facilities, this
 factor  should be considered in site selection.

      The basic requirement  for almost  any geographical  location  is to con-
 struct  a site that is usable by  heavy  equipment on a year around basis.
 The site should be well drained  and in most  cases this  drainage  should be
 collected to  a holding pond.  Suitable facilities should be provided for
 administration,  testing, equipment storage,  and maintenance.  Access should
 be  provided to all working  areas and this access  should be  suitable  for
 heavy equipment.  The minimum construction for  this  access  should  be gravel,
 but paving  is better.

      All working areas should be heavily gravelled as a minimum.   It has
 been  demonstrated at Beltsville  that regular year around operations  can be
 carried out on crushed stone, but drainage,  cleanup, and other working con-
 ditions  are less than optimum.   Also,  it is  impossible  to keep the gravel
 out of  the  materials  and some heavy metals can  be leached from some  types
 of  gravel.  All working areas should be  well drained because runoff  from
 the composting process  is significant.   Removal of runoff will help  to keep
 the materials  as dry as possible and minimize odors and nuisance problems.

      Properly designed hard  surfaced work areas will provide more  satisfac-
 tory  operations, better drainage,  and will facilitate cleanup.   The  compost-
 ing area should have  highest priority  for paving,  however,  the screening
 area  is  also  important.  If necessary, the bulking agent and compost storage
 areas can be  operated satisfactorily without paving.  It is recommended
 that  reinforced  concrete surfaces  be provided,  however, asphaltic  cement can
 be  used.  The  asphaltic cement is  more prone  to damage  from equipment be-
 cause it tends to soften during  hot weather  and from heat under  the  compost-
 ing piles.

WEATHER

     Weather  can have  a significant effect on composting operations  and must
be taken  into  consideration both in design and  in carrying  out operations.
 It is possible to carry out composting operations  under nearly all weather
conditions  as  demonstrated at Beltsville, Bangor,  and Durham, but  experience
has provided many useful observations.   Significant adverse weather


                                     20

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 conditions  are  snow, rain, cold  (below  freezing), inversion conditions, and
 high winds.  The effects of each of these conditions on composting will be
 discussed along with methods for mitigating the  adverse effects.

 Cold Weather Operations

     Generally, cold weather above freezing has  little effect on composting
 operations, therefore, this section will relate  to locations with extended
 periods of  subfreezing weather.  Conditions where temperatures dip below
 freezing occasionally or at night, but  return to above freezing during the
 day are of  little concern.

     While  extremely cold temperatures  do have some adverse effect on the
 compost pile process performance; Beltsville, Bangor, and Durham have demon-
 strated that the composting process can perform well in very cold climates.
 Extra care  is needed in mixing, pile construction, and covering to assure
 optimum performance.  Most cold weather problems relate to materials hand-
 ling and equipment.  Equipment will be  harder to start in cold weather
 (especially diesel engines), but this can be mitigated by installing block
 heaters and storing equipment inside.   Equipment operator stations should
 be enclosed and heated for cold weather operations.  Equipment service and
 maintenance is more difficult and suitable arrangements should be made for
 carrying on regular and emergency maintenance.

     Materials handling problems relate primarily to freezing of these
 materials.  Generally, because of the heat generated, freezing of the com-
 posting piles, unscreened compost, or screened compost even in very cold
 weather has not been significant.  Freezing of the bulking agent can be a
 problem.  The wood chip bulking agent used at Beltsville does not freeze
 into large  chunks because the moisture drains well from the material.  Re-
 cycled wood chips do freeze to some extent because of the additional mois-
 ture and smaller particle size.  Bulking agents which hold moisture will
 tend to freeze, however, the bark at Bangor only freezes on the outside,
 and heat is generated inside the piles.

     Screening when temperatures are below freezing is a problem.  The
 mechanical parts of the screen freeze and a residue freezes on the screen.
 Screening is not undertaken when it is below freezing at Beltsville and
 Bangor.   In other cold locations it would be possible to stockpile unscreen-
 ed compost during freezing weather and only screen when the temperature is
 above freezing.  The other alternative would be to screen in a heated space
 or screen during freezing weather and try to overcome the problems.  Ade-
quate screening capacity must be available so that all required screening
 can be performed during the available suitable weather for a particular
 location.


     The extremely cold weather in Bangor has a noticeable effect on the com-
posting process.  It is difficult to pinpoint the exact cause of the prob-
 lems.   City personnel report that if the sludge-bulking agent mixture can
be kept above 4°C the pile has a much better chance of performing well than
 if the mixture temperature drops below  4°C.  If wet bulking agent is used or
 if mixing takes place in rain the resulting compost pile may not perform well.


                                      21

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      Bangor personnel are testing various methods  of improving cold weather
 operation such as reusing unscreened compost as  bulking agent  (use of heat
 in the compost),  piping the  warm air discharge from an  older composting pile
 into the new pile initially,  and using a heater  to warm the air blown into
 a new pile.   It is too early to develop conclusions except that
-------
 considered in planning plant operations  and designing facilities  for  sludge
 storage at the plant.   Generally,  however,  the  effects of snow on the pro-
 cess are minimal.

 Inversion Conditions

      The composting operations do  generate  mild odors at times and may be
 most noticeable during inversion conditions with light winds.  Careful
 operations will minimize odor generation.   Slight odors were noticed  at
 Beltsville under inversion conditions, but  the  problem was very minor and
 complaints are nil.

      Odors were also noticeable at the Bangor composting site.  These odors
 might be considered unacceptable to some people visiting the actual site.
 Apparently, these  odors are dispersed rapidly away from the site  because
 outside complaints have not been received.   The site  is about 2,000 feet
 from the Bangor International Airport terminal  building and about a like
 distance from a major  shopping center.

      The normal operations at Beltsville and Bangor have never been shut
 down due to odor generation.   There is no easy  way to shut down a composting
 operation in any case  because it is a continuing process involving large
 quantities of "active" materials.   The best safeguard is to conduct careful
 operations, but odors  will occasionally  be  generated.  Beltsville does have
 both mobile and fixed  deodorizing  equipment which is  used infrequently.

 High Winds

      It is possible that areas with significant prevailing winds  may  have
 problems with blowing  of materials, especially  with light bulking agents,
 and dust.  The best mitigation would be  careful site  selection and masking
 of the site with wind  barriers such as trees.   In most areas, materials
 handling operations can be suspended during occasional periods of high wind.
 Dust can be controlled by careful  site cleanup  and the use of water.

 Summary of site Considerations

      Operations downtime at Beltsville was  minimal during 1976.   Regular
 sludge deliveries  have been accepted on  schedule except when the  Blue Plains
 Plant was unable to provide sludge or trucking  was impossible.  During the
tsevere weather of  January 1977 sludge was accepted five days a week on
 schedule.  Downtime at Bangor in 1976 was slight and  due mostly to schedul-
 ing of public works department personnel.   Downtime should be reduced even
 more now that the  treatment plant  is providing  the personnel.  No on-site
 sludge storage is  available at either composting site and it is recommended
 that such storage  be limited to the wastewater  treatment facility. As far
 as can be determined no nuisance complaints were received as a result of
 normal Beltsville  and  Bangor operations.

      The essential function of compost pile formation has been performed
 on a regular schedule  with little  disruption.  Other  operations with  more
 flexibility such as screening have been  performed when conditions are


                                      23

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 favorable, but  still have met the needs of the overall operation.  Waste-
 water sludge composting has been demonstrated on a regular schedule for over
 two years at each site completely outside.

     The hard surfaced composting pad at Beltsville will not reduce "down-
 time" or decrease the costs of operation.  The primary advantages relate to
 more satisfactory and orderly working conditions.  Drainage is much more
 satisfactory and cleanup is much easier and more complete.  Water drainage
 from the composting pile is probably much more satisfactory, but the econo-
 mic effect is almost impossible to calculate and probably quite small.

     A portion of the new Beltsville covered area will be reserved for
 equipment maintenance.  The balance of the covered area will be used for
 composting operations; primarily research and demonstration.  The covered
 area will not reduce operational "downtime" but will provide additional data
 related to composting without the effects of precipitation.  It is antici-
pated that the covered area will have little direct effect on normal
operations.  The cost of the Beltsville covered area is approximately $10
per sq ft including the concrete slab.

     The primary adverse weather effects at operating installations are
summarized as follows.

     Cold
     - equipment starting and operation are more difficult.
     - equipment service and maintenance requires appropriate facilities.
     - equipment cabs must be enclosed and heated.
     - freezing of bulking agent may be a problem.
     - screening is difficult to carry out.
     - composting pile initial heat generation may be slow in extreme cold.

     Rain
     - site and working area drainage is important.
     - runoff collection and treatment must be considered.
     - moisture absorption during sludge-bulking agent mixing and pile
       formation must be minimized.
     - moisture absorption by unscreened compost prior to screening can be
       a problem.
     - screening is  difficult to carry out.

     Snow
     - generally,  similar to rain,  but less  severe.
     - visibility problem.
     - site  clearing and access  is  necessary.

     Inversion  Conditions
     -  little documented problem under this  condition.

    High Winds
    - blowing materials and dust can be problems.
                                     24

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NUISANCES

     The potential nuisances of a raw sludge, forced aeration composting
operation are:

     1.   Sludge hauling
     2.   Visual objections
     3.   Odor generation
     4.   Vermin propagation or attraction
     5.   Noise

     No known nuisance complaints have been traceable to raw sludge cake
hauling at Beltsville or Bangor.  It is desirable to locate the composting
site as close as possible to the treatment facility thus further reducing
any potential for nuisance problems to develop.

     A composting site is a potential visual nuisance because of the large
piles of materials and heavy equipment.  The Bangor site is in plain view
to people using the Bangor International Airport, but complaints have not
been teceived.  A better approach is to mask the site from view by careful
selection or landscaping if possible.

     Odor generation is potentially of great concern because some mild odors
are generated at composting sites; yet, no complaints have been received at
Beltsville or Bangor.  odors have been noticeable at the Bangor site, but
are not noticeable off the site.  The best solution is to use care in
selection of the site and, perhaps, have mobile deodorizing equipment avail-
able for use.

     No rodent, fly, or other vermin problems have been reported at Belts-
ville.  Bangor did report some fly problems in 1976 and 1977.  During the
1976-1977 winter, mice have been nesting in the curing piles and it is not
known if this will be a problem.  To date, the reported and observed vermin
problems seem to be minor to non-existent.
                                     25

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                                 SECTION 4

                    CONSIDERATIONS FOR FUTURE OPERATIONS
 GENERAL

      Actual forced aeration composting operations to date  have  demonstrated
 the ability to process undigested wastewater sludge cake into a useful  com-
 post product with minimum on-site nuisance and essentially no public  com-
 plaint.   It is probable that further  modifications and improvements to  the
 process will provide additional  operational advantages and reduction  in
 cost.

      A number of these possibilities  are  outlined in this  section, but  it
 is  emphasized that process modifications  should be tested  under carefully
 controlled conditions to prevent the  possibility  of on-site and off-site
 nuisances  and public complaints  in the  event that some are unsuccessful.
 The type of operation most advantageous in a given situation  will depend on
 the goals  of the operation,  the  market  for compost,  available bulking
 agents,  climate,  and similar considerations.

 MATERIALS  HANDLING

     This  is probably the  most significant factor in the composting opera-
 tion;  it is a materials  handling operation.   A study at Durham,  New Hamp-
 shire (1) investigated the  use of fixed  materials  handling  equipment as
 compared to the  mobile equipment now  used  almost  exclusively.   The study
 concluded  that certain steps  in  the operation could  be mechanized to  advan-
 tage,  specifically,  the  sludge-bulking  agent  mixing  and movement of some of
 the materials using  conveyor belts.   The design for  Camden, New Jersey  is
 reportedly based on  extensive use  of  mechanized fixed  materials  handling
 equipment.

     Mechanization using fixed equipment has  not  been  demonstrated, except
 that conveyors are presently used  to  move  materials  within  the  screening
 process.   The  present practice of  using mobile equipment provides greater
 operational flexibility, but may increase  some other operational costs  such
 as  labor.   The flexibility required for a  composting operation  should re-
 ceive  careful  consideration, particularly  when planning the materials
 handling operations.

     There  is a need  to  realistically evaluate various  modes  of  operation
and  the effect on materials quantities  to  be  handled in order to minimize
the costs of materials handling.
                                     26

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BULKING AGENT

     The bulking agent is a prime consideration in the composting process
because it can be a major cost item and may be difficult to obtain in cer-
tain parts of the country.  The exact considerations relating to bulking
agent are site specific, but, it is possible to develop some general con-
siderations.

     It is important to plan for the bulking agent in the early stages of a
wastewater sludge composting project to assure a supply of suitable mater-
ial and for the materials handling equipment.  Thereafter, in most cases,
it is desireable to minimize the need for additional material because of the
cost.

     It is possible to recover approximately 70 to 80 percent of wood pro-
duct bulking agent used in construction of a pile by screening after comple-
tion of the composting or curing process.  This recovered bulking agent can
be reused and removal of this material from the compost helps to increase
the volumetric nutrient content of the final compost product.

     It also may be possible to use the compost from a pile being torn down
as the bulking agent for a new pile.  This is illustrated in Table 8 and
has been demonstrated in practice at Bangor with satisfactory results.  In
fact, Bangor has reused compost through two additional compost cycles (in
addition to the original pile) as bulking agent with satisfactory results.
As illustrated in Table 8, this procedure reduces both the bulking agent
and screening requirements significantly along with other key process mater-
ials handling requirements.  This can be significant for operations trying
to minimize costs and illustrates the significant effect that can be obtain-
ed by varying operational procedures.

     A number of other materials have been used as a bulking agent such as
shredded tires, peanut hulls, cubed solid waste, and licorice root.

SCREENING

     Screening is one of the more difficult and time consuming operations
related to composting.   Ideally, it would be desireable to eliminate
screening if a market could be found for coarse compost and/or if an inex-
pensive bulking agent could be found that would essentially disintrigrate
during composting and curing.  Elimination of screening would, however,
increase the requirement for new bulking agent.  Practically, one solution
is to develop a good balance in operations so that screening is limited to
a manageable level of effort.

     The best experience to date has been with horizontal, rotary type
screens with a screen opening of 1/4 to 1 in.  An effective drum screen
should be about 10 to 15 ft long to provide adequate tumbling action to
separate the fine and coarse particles.  Shorter screens have been used,
but particle separation is not complete and the recovered bulking agent
contains fines.  Feed rates must also be controlled to achieve good perfor-
mance.  Moisture content is a significant factor, but the horizontal screen

                                     27

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has demonstrated an ability to operate even with relatively wet compost  (up
to 50 or 55 percent moisture).  Vibratory screens have been satisfactory for
moisture contents up to 45 percent.

     With careful planning of operations it may be possible to reduce screen-
ing requirements significantly as illustrated in Table 8.  Unless a covered
area is available, screening can be carried out only in good weather and
then the daily production must be carefully evaluated because of downtime,
maintenance, and other factors.  Screening capacity could be a limiting
factor unless the capacity is carefully selected in relation to volume of
materials to be screened.  Screening typically requires one man plus a
front loader and operator.

     It is also possible to reduce screening by marketing some compost un-
screened, but this will increase bulking agent requirements.  It may also
be necessary to market some compost unscreened if space is not adequate to
store materials during times when screening cannot take place.

SITE WEATHERPROOFING

     A permanent composting site should have certain basic amenities.  The
first would be a hard surfaced working area (preferably reinforced concrete)
for mixing and composting.  Other areas such as roads, materials storage
and the screening area should be covered with a thick layer of crushed
stone as a minimum though paving would be more satisfactory.  Mixing, com-
posting, and curing areas should be well drained to adequate runoff
collection and storage facilities.

     Beltsville and Bangor have demonstrated that covered areas are not
necessary to carry out continuous operations.   In some climates, covered
areas would be helpful for:   (1)  protection of bulking agent, (2) protection
of curing compost, and (3) protection of the screening area from rain.

     Covered composting pads would possibly contribute to more satisfactory
composting in very wet or cold climates, but there are no data available
to give a quantitive comparison at this time.
                                      28

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                                SECTION 5

                           COMPOST DISTRIBUTION
GENERAL

     Compost has been distributed from the Beltsville operation for several
years.  Reportedly, all of the production has been distributed in the past
without satisfying the demand.  Most of the compost is provided free of
charge to various public agencies who pick the material up at the Beltsville
site.  Some compost has been sold for $1.00 per cu yd (approximate weight
850 Ib per cu yd) to private companies (not individuals).  Part of the com-
post is screened prior to distribution, and some compost is also distribu-
ted unscreened.

     Compost from the Bangor operation has been stock piled.  A marketing
program began in Spring, 1977.  The policy is to market the compost for
approximately $1.00 per sack (approximately 60 to 80 Ib), $5.00 per cu yd in
bulk, or $10 per bulk pickup load.  The compost is picked up at the site by
the user and is loaded by City personnel.  The City is also considering
promotional efforts through other outlets such as supermarkets and nurseries
in addition to sale to other City Departments such as Parks.

USES

     There are a number of identified end use options for wastewater sludge
compost:

     1.   Base for potting mixes.
     2.   Bedding mix for flowers.
     3.   Planting mix for trees and shrubs.
     4.   Base for producing "on-site" topsoil.
     5.   Surface mulch (although this is not recommended by all
          authorities).
     6.   Base for reclaiming mined or other unproductive areas or soils.
     7.   Land reclamation.
     8.   Landfill.

DEMAND

     No formal studies have been undertaken in Bangor to determine potential
demand for the compost.  The City has nevertheless decided to sell the com-
post and has disposed of approximately 80 to 100 cu yd in 1977 through the
month of May, compared to annual production in excess of 4,000 cu yd.  it
                                     29

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is very difficult to determine the total volume that can be disposed of in
the Bangor area.  The season is very short and there is very little poten-
tial demand in the winter.  Adequate space is available for storage of
large quantities of compost during the winter or from year to year.  Until
the market for compost can be developed in the Bangor area, the best
strategy is to minimize compost production through appropriate operational
strategies as illustrated in Table 8.  It is likely that all of the Bangor
compost could be landfilled at the present sludge disposal site, but this
method of disposal does not meet the City goal of realizing some revenue
from the disposal of the compost.

     A comprehensive study^ was recently completed which projected compost
demand in the Washington, D. C. Standard Metropolitan Statistical Area
(SMSA) and within a 100 mile radius of Washington, D. C.  Estimates of
demand, considering certain restrictions on use, ranged between 5,600 and
161,000 tons of compost per year within a 100 mile radius of Washington,
D.C.  Although this is a broad range, it indicates a potential market for
the forseeable production from the Beltsville site.  Production at Belts-
ville would be approximately 20,000 tons of compost per year if all the
compost were screened, through  actual production is somewhat higher because
some compost is not screened.

     Other wastewater agencies within the Washington, D. C. area are con-
sidering composting and this would increase the quantity of compost
available for distribution.
                                     30

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                                 SECTION 6

                                   COSTS
      Composting costs  are  documented  for both  Beltsville  and Bangor.  The
 Beltsville costs must  be considered carefully  because  they include allow-
 ances for various research activities and  the  equipment and site may be
 capable of handling 2  to 3 times more sludge than  is presently processed.
 a"1™* fn^nCial aspects  of  <** Beltsville operations are shown in Table
 9.   The 1976  actual and projected  1977-1978 costs  were developed from in-
 formation provided by  MES  for the  total operation  including research; but
 do  not include  the amortization of equipment or  site costs.  The off-site
 administrative  cost item is basically unrelated  to site operations.  The
 on-site labor cost includes site supervision.  Sludge  hauling cost is for
 contract transport of  sludge  cake  from the Blue  Plains Plant to the compost-
 ing site.   These hauling costs are site specific for the  Beltsville opera-
 tion.   Costs  for bulking agent may not reflect actual  usage because chips
 are purchased when prices  are favorable and large  quantities can be stock-
 piled.   Screening in 1976  was performed by outside contract, however, all
 screening is  now performed using on-site labor.  The projected Beltsville
 costs  for 1977-1978 were modified  to  show  two  different sludge input rates
 and research  related costs were removed.   Individual breakdown of costs for
 various processes such as  mixing,  pile construction, and  screening are not
 available  from  Beltsville.  However,  cost  estimates were  prepared for an
 Smltr  ^    **5 Beltsville based on time  and  motion  study at Belts-
 ville^.   This  study  estimated that  total costs,  including capital amorti-
 zation,  are approximately  $51 per  dry ton  of sludge cake  solids for an
 operation processing 10 dry tons of sludge solids  per  day.  Total capital
 costs  for  site  improvement and equipment were  estimated at $376,000.  Esti-
 mated  costs for  50  dry tons of sludge solids per day were $36 per dry ton,
 including  amortization of  approximately $1,500,000 of  capital costs.  Costs
                                                                     may be
     Bangor operation costs for 1975 <4> are shown in Table 10.  The capital
investment was very low because only minor site work was required.  Equip-
includH,                  P001'  totization of equipment is
included in the hourly equipment charge under "Operations".  Cost informa-
tion is not available for 1976.  An estimated breakdown of labor and
equipment requirements by operation is shown in Table 5.
 i H Pr!o!Snary f timates at Durham indicate a cost of $16.00 per cu yd of
sludge  ($107 per dry ton solids for 20 percent solids sludge) <5? for J^_
posting an estimated 200 to 250 dry tons of sludge per year excluding
                                     31

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                                 TABLE 9.  BELTSVILLE ACTUAL AND PROJECTED COSTS
CJ
to
Estimated Costs**

Off-site
Admin. , of f -site
On site operations
Telephone & travel
Utilities
Fuel & oil
Sludge hauling
Labor incl. fringes
Misc. contract services
Wood chips
Supplies & materials
Equipment insurance
Total
Total excluding off-site
Dry tons sludge per year
(23 percent solids)
Annual cost, $/dry ton
sludge solids
Projected
Oct. 1977-Sept. 1978

$ 60,000

1,300
2,211
10,500
132,000
125,750
27,540
144,000
22,250
4,000
$529,551
$469,551

3,450

$136
Actual
1976

$ 46,501

3,971
426
13,036
120,000
152,919
112,942*
73,145
32,176
3,955
$559,071
$512,570

3,450

$149
18,200
wet tons/yr****

-

1,300
2,211
10,500
-
80,000
27,540
144,000***
22,250
4,000

$291,801

4,200

$ 69
45,500
wet tons/yr

-

1,300
3,000
25,000
-
125,750
37,000
350,000***
35,000
4,000

$581,050

10,500

$ 55
     *    Includes screening performed by outside contract, screening now performed on site by MES personnel.
     **   Excluding requirements of research work.
     ***  Assume 50 percent of compost marketed unscreened and 70 percent recovery of bulking agent after
          screening finished compost.
     **** Present rate of 350 wet tons of sludge per week.  Reported capacity of site is 875 wet tons of
          sludge per week.

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             TABLE  10.  BANGOR COMPOSTING COSTS, 1975-1976(4)
           Capital amortization
             6 percent, 5 years        $  3.00*

           Operations                    43.00

           Bulking agent                 37.00

           Analysis                       3.QQ

                                      $ 86.00
   *Costs per dry ton of sludge for a total of 525 dry tons
    per year.
capital amortization.

     The major cost items at present composting operations are labor and
bulking agent which can each be 30 to 45 percent of the total annual cost
of composting.  Operation and maintenance of the mobile equipment at
Beltsville, excluding capital amortization and direct labor, is 10 percent
or less of the total annual cost.   Amortization of the purchase cost of the
equipment at Beltsville (approximately $400,000} over six years a?7 pfrcent
would be approximately $84,000 per year or about 13 to 23 percent of total
annual costs shown in Table 9 depending on the case.      ^ercent or tocai
                                    33

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                                 SECTION  7

                                 PATHOGENS
      Data  are  available from several  sources  (Table  11) that indicate path-
 ogen  and/or  indicator organism density in composted  wastewater sludge at
 various  stages of  the process.  The total and fecal  coliform, and salmonella
 data  are summarized  in Table 12.

      Sufficient data are available from Bangor to plot cumulative probabil-
 ity curves of  bacterial densities in  sludge, compost/ and compost stockpile.
 These curves (Figures 3, 4, and 5) are plotted to a  lower density of one log
 (base 10)  cells per  gram which also include all densities below this level.

      Although  data vary widely, they  are consistent  in that some measureable
 level of salmonella, fecal coliform,  and total coliform can be present in
 composted  wastewater sludge.  In most cases, especially in the static pile
 composting method, salmonella densities were below detectable levels,
 and when detected  were less than one  log cells per gram.  No salmonella have
 been  detected  in compost samples at Bangor in over a year, although salmon-
 ella  were  detected in compost samples in early 1976.  Total and fecal coli-
 form  densities up  to 5 or 6 log cells per gram have  been detected, but
 typically  the  levels are below 3 or 4 log cells per  gram in the finished
 compost.

      A study has reported on survival of virus through the windrow compost-
 ing process, particularly the F2 bacterial virus(7K  This work indicates
 reductions in  densities to less than  one or two log  PFU per gram with win-
 drow  composting and  stockpile curing.  It is expected that greater reduc-
 tions in virus concentrations would be observed using the static pile
 method because higher temperatures are developed.

      Data  indicate that maximum temperatures achieved by static pile com-
 posting  even during  very cold weather are generally  greater than 60°C for
 at least a day and usually for several days.  Exposure to temperatures of
 60°C  for a period  of a day or two will inactivate  most pathogens.  Temper-
 atures are not uniform throughout the pile and temperatures near the outside
 of the pile  may be significantly below 60°C and not  great enough to inacti-
 vate  all pathogens.  Tests have shown that indicator organism densities vary
within the pile.   It is possible to inactivate virus, bacteria, protozoa,
 and helminth by subjecting all parts of the composting mass to lethal tem-
peratures.    With present procedures it is not possible to assure total
 inactivation using outdoor composting methods because organisms may survive
near  the surface of  the piles while total inactivation may be achieved
                                     34

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                   TABLE 11.  SOURCES OF PATHOGEN DATA
Location
Type of composition
                                                           Reference
Beltsville, MD

Bangor, ME

General
Windrow and Static Pile

Static Pile

Windrow and Enclosed
   (6)

Plant Records

   (7)
                   TABLE 12.  SUMMARY OF BACTERIA DATA
Location
    Range of reported densities

    	cells/gram of compost	

 Salmonella  Total coliform    Fecal coliform
Beltsville, MD6
     Highest                
-------
2
(9

2

IU

o
o
                                                            —  SUMMER COMPOST
                     10     20    30   40  SO   60   70    30      90     95     98     99






                        PERCENT OF MEASUREMENTS BELOW INDICATED LEVEL


                                Developed from data from Bangor, Maine
                    Figure 3.  Total  coliform densities.
                                         36

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(9


3
UJ
u
o

3
              5     10     20    30   40  50
                                              60   70    80      90   95     98    99
                       PERCENT OF MEASUREMENTS BELOW INDICATED LEVEL


                               Developed from data from Bangor, Maine
                     Figure 4.  Fecal coliform densities.
                                        37

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(9

3
UJ
O   4
(9
O
            Anr
ual o
        :i impost
suiimer a: id wint
reflects
»r percen
he
lie
                                            WINTER COMPOST
                                                   ANNUAL COMPOST
combined
 levals
                                                    aver
                    10
           20   30    40  50   60   70   80
                                                  90     95    98    99
                       PERCENT OF MEASUREMENTS BELOW INDICATED LEVEL.

                             Developed from data from Bangor, Maine
                      Figure  5.   Salmonella  densities.
                                       38

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within the pile.  Therefore, it must be assumed that pathogenic organisms
will survive the composting and curing processes unless some means of posi-
tive sterilization is used.  Although the measurement of indicator organism
density in the compost may not be a reliable method to determine actual
levels of pathogenic organisms it is possible to apply historic ratios of
pathogens to indicators to develop some generalizations of the risk of
illness.

     Hornick, et al'9' recently published dose - response data for Salmon-
ella typhi bacteria.  These data indicate that the dose required to cause
typhoid fever in humans was quite high (see Table 13).  Earlier work^10^11*
(12) has also shown that large doses of other species of Salmonella are re-
quired to cause significant human disease (see Table 14).

     Methods have been developed for estimating the disease risk based on
the indicator organism density in drinking water<13)(14)(15).  while these
methods have been developed for ingestion of drinking water, they can be
applicable to ingestion of sludge.  The major difference is that normally
only small amounts of sludge or compost would be ingested as compared to
water.  Data from Mechalas, et al(15) is shown in Figure 6, and provides the
basis for the illustration that follows.   For purposes of illustration,
assume that a compost marketed to the public contains a total coliform count
of 10  organisms per gram of compost and that one gram of the compost is
ingested by a human adult.  The human would have ingested 103 indicator
organisms.  One gram of compost would be approximately 2.0 ml in volume at
850 Ib/cu yd.

     According to Figure 6 the risk of illness would be approximately one
in 1,000,000 by extrapolation of the curve (approximately 5 x 104 MPN/100
ml total coliform).  Based on earlier work by Kerr and Butterfieldd3) in
estimating relationships between numbers of indicator organisms and disease
organisms in wastewater, a rate of, say,  100 salmonella of all types per
1,000,000 coliforms would be very high.  Therefore, for the 103 coliforms
ingested it is quite likely that less than one salmonella would be ingested.
Typical coliform to virus ratios would be 50,000 to 100,000:1(8) and, there-
fore, for 103 coliforms less than one virus would be ingested.  It has been
shown for both virus and salmonella that significant numbers must be in-
gested to cause disease in humans; typically over 103 salmonella  (of most
types).  Small doses of virus typically produce infection but not disease
in humans.

     This logic indicates a very low risk in using properly composted
wastewater sludge even though it is not possible to assure complete kill of
pathogenic organisms using outdoor composting techniques.  At the level of
coliform organisms found in typical wastewater sludge compost and assuming
normal disease rates within the community, it is highly unlikely that
enough of this compost would be ingested to produce disease in adult humans.
Infants may be more susceptible.  However, the danger of disease outbreak
is very small considering the volume of compost that would normally be in-
gested.  Also infants are less likely to be exposed than adults.
                                     39

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             TABLE 13.   RELATION OF DOSAGE OF SALMONELLA TYPHI
                        TO DISEASE
                        (From Hornick et al.) *9'
  No.  of viable                 Total volunteers            Number
 Salmonella typhi                 challenged          with disease  (percent)

g
ioy
O
10b
•7
107
c
105
•3
103

42

9

32

116

14

40

8

16

32

0

(95)

(89)

(50)

(28)

(0)
      Use of wastewater sludge compost does entail some disease risk, but
 for  typical compost with total coliform counts of 10^ to 10  cells per
 gram, the  chance of disease outbreak in humans is probably less than 1 in
 1,000,000.   Should an area be subject to outbreak of a particular disease
 then the risk of infection from compost would be higher because of the pre-
 sence of additional pathogenic organisms.

     A potential problem recently observed at the Beltsville composting
 operation is the possible presence of secondry pathogens, specifically
 fungi.  In the composting process fungal growths can proliferate, particu-
 larly at too low a composting temperature in some part of the pile, or by
 reinfection.  In fact, much of the action of composting is probably due to
 fungal organisms.  Some fungi, for example Aspergillus fumigatus, can pro-
duce toxic effects in susceptible individuals.  Excessive concern is not
warranted, but it is advisable that individuals with lung ailments or
asthma not be exposed in the composting plant.  Dusty conditions should be
avoided, or dusk masks worn when dusty conditions cannot be avoided.
                                    40

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       TABLE 14.  DOSE OF VARIOUS SPECIES AND STRAINS OF SALMONELLA
                  THAT CAUSED DISEASE IN HUMAN VOLUNTEERS
                  (From McCullough and Eisele) (1°)
  Salmonella                                 Dose at which 50% or
species/strain	 more develop clinical disease

S. meleagridis 1                                   50,000,000

S. meleagridis 11                                  41,000,000

S. meleagridis 111                                 10,000,000

S. anatum 1                                           860,000

S. anatum 11                                       67,000,000

S. anatum 111                                       4,700,000

S. newport                                        .  1,350,000

S- derby                                           15,000,000

S. bareilly                                         1,700,000

S. pullorum 1                                   1,795,000,000

S. pullorum 11                                    163,000,000

S. pullorum 111                                 1,295,000,000

S. pullorum IV                                  1,280,000,000
                                    41

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     0.010

     0.001
    0.0001
          10'
            ,-1
          103
        4.9x10*
                          I
  10°

   I
  104

   I
6.8 xlO3
                                  I
    01             102
     SALMONELLA/LITER

    I       	I
   10a
106
                                        COLIFORM.MPN/lOOml
 6.Bx104         7.0 xlO5

FECAL COLIFORM, MPN/100 ml
               103
 10?

J
                 106
Figure  6.   Relationship between disease  risk and salmonella,
            coliforms,  and fecal coliforms  (after Mechalas et al.).
                                     42

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                                SECTION 8

                          RESULTS AND DISCUSSION


     Operations at both Beltsville and Bangor have demonstrated that com-
posting operations ca'n be conducted outdoors on a year around basis even
in extremely cold climates.  Both sites have been in use for static pile
composting for over one year on a continuous basis.  Operations were ob-
served at both sites during all types of weather as shown in Table 1 for
the purpose of analyzing various aspects of the operations under all weather
conditions.  The materials handling operations can be conducted outdoors
using readily available mobile equipment under all weather conditions en-
countered at both sites by proper scheduling of work.  It may be possible
to use fixed materials handling equipment for portions of the materials
handling operations, but this has not been demonstrated on a full scale
operation.

     Both operations are continuous on a year around basis; Beltsville re-
ceives limed sludge cake on a 5 day a week schedule and Bangor once a week
and, occasionally, twice a week.  Sludge is not stored at the composting
sites, but is brought to the site when it can be handled and formed immed-
iately into compost piles.  The open operations are vulnerable to precipi-
tation during the sludge-bulking agent mixing process, but once formed into
piles the precipitation has little effect.  Mixing can be accomplished in
the rain at Beltsville because they have the equipment to accomplish the
operation quickly.  Bangor, on the other hand, can not mix during rain and,
therefore, they schedule mixing on favorable days.  Sludge can be stored at
the plant to allow this flexibility in scheduling.

     The major impacts of weather on outdoor composting operations are
summarized as follows:

     1.   Rain
          - Screening can not be conducted in the rain without cover.
          - Moisture absorption by unscreened compost stored outdoors
            may make screening difficult or impossible during and follow-
            ing periods of rain.
          - It may not be possible to conduct sludge-bulking agent mixing
            during rainy weather unless the mixing can be accomplished
            rapidly.
          - Some bulking agents may absorb excessive moisture during rainy
            weather when stored outdoors.
                                     43

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      2.    Extreme  Cold
           -  It is  necessary  to  conserve  heat as much as possible in order to
             maintain  optimum composting  performance.  Bangor has developed
             several procedures  such  as using warm  compost  from an active
             pile being  torn  down  as  bulking agent  for mixing and construc-
             tion of a new pile  and/or piping hot exhaust air from an active
             pile into a new  pile  for the first few days and using relatively
             heavy  covers of  compost  over the piles as insulation.
           -  Equipment cabs must be heated and covered maintenance areas must
             be provided.  It is advantageous to store equipment inside when
             not being used.

      3.    Snow
           -  Snow has  not been a serious  problem except for impeded visibil-
             ity and need for site clearing.

      4.    High Winds
           -  High winds  can cause materials to blow and can cause dust con-
             ditions.

      5.    Inversion Conditions
           -  Inversion conditions have not caused problems at either site
             during operations.

      Weather conditions have not caused  "down time" at either site and, in
 fact  it is not possible to "turn off" composting operations.  Both sites
 schedule operations on  a regular year-round-basis.  Certain site improvements
 are necessary  or can  facilitate easier operations, but may not decrease
 costs significantly.  The site  improvements considered mandatory are heavy
 crushed stone  cover so  that  heavy equipment can operate year around.  A
 crushed stone  surface has many  limitations, but can be used as demonstrated
 at Beltsville.  More  desireable and  almost in the  mandatory category would
 be hard surfacing  (preferably reinforced concrete) for access roads and the
 mixing and composting areas.  Of lesser  importance would be paving of
 screening  and  storage areas.  Covered areas for mixing, screening, and un-
 screened compost storage would  be helpful in areas with high precipitation.
 Covered composting areas may be helpful, but are not considered necessary
 in most climates.

      A covered  area under construction at Beltsville will be used for re-
 search studies.  The  normal work areas will not be covered.  A.paved mixing
 and composting pad was constructed and placed in service for regular oper-
 ations.  While  this pad is a  significant improvement over the crushed stone
 surface it was  not installed  because of  expected operational cost savings.
 The advantages of the pad are less stone pickup in the compost, better
 drainage and easier cleanup.

      There have been  no significant  nuisance complaints at either site.
 Some  odors are noticeable at  both sites.  Beltsville has an odor control
 system, but is  is seldom used.  Paved work areas would help reduce odors on
 site because the compost and  sludge  can  work down  into the crushed stone.
Operations have never been shut down at  either site during static pile


                                     44

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composting because of odor generation.  Some fly problems have been noted at
Bangor, but only around composting piles.  Good site drainage and housekeep-
ing will minimize fly problems.  Both sites have occasional problems with
blowing materials and dust, but just on the sites.  Beltsville uses a water
wagon to help reduce dust from equipment operations during dry weather.
Paved work areas also would help reduce the dust problem.

     Various weather conditions have had no documented effect on manpower
or on the material quantities processed at either site.  Some operations,
such as screening, have to be curtailed during rain but equipment is sized
so that screening can be accomplished during good weather.  At Bangor, man-
power is scheduled as needed, but at Beltsville the same level of manpower
is available year around.

     It is significant to note that savings can be made in manpower and
materials handling by developing an optimum operation for a particular site
and situation.  This is illustrated in Table 8.  By changing the bulking
agent to unscreened compost the amount of screening and the volume of
make-up bulking agent can be reduced significantly.  This is only one exam-
ple of possible savings for a cost conscious municipal operation.  It is
anticipated that other significant cost savings can be made by varying
operations and, in fact, the potential savings are greater than those that
may be realized by weatherproofing the site.  Additional study is needed to
find ways to reduce composting operation costs.

     The product quality is affected very little by weather at a well run
wastewater sludge compost operation.  Available pathogen data do indicate
some minor improved kills in summer above the high kills generally achieved.
No data are available on seasonal volatile solids reduction.  Color is a
function of moisture content and is not a reliable indicator of process
efficiency or performance.  Odor is not affected by season or weather con-
dition as best can be determined.

     Pathogens and indicator organisms may be present in finished compost
and there is no solution to this problem except complete sterilization.
The outside of the piles may not reach lethal killing temperatures and
therefore, some organisms can survive.  A risk analysis based on data from
Beltsville, Bangor, and published data indicates that the health hazard to
adult humans is very slight.  The methods used herein can be applied to
specific situations for estimating risk to public health.

     If the composting site is well laid out with specific separated areas
for mixing,, composting, screening and storage, and if proper procedures are
used for mixing, composting, and curing, it is extremely unlikely that raw
sludge or improperly composted sludge can become mixed with finished com-
post and delivered to users.  It is possible to use pathogen or indicator
organism analysis as a basis for quality control.  However, it is felt
that this type of sampling and testing is not convenient and can be costly
for most smaller municipalities.  This type of testing can be used for spot
checks.  Probably the most-useful control is regular temperature monitoring
of the piles.  Temperature monitoring is simple, quick and provides a re-
liable indicator of day to day pile performance so that necessary process


                                    45

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changes can be made quickly.  Daily monitoring is desirable, but perhaps
monitoring every few days will be more practical for most operations.   Based
on past operations at Beltsville and Bangor, if inside pile temperatures stay
above 60°C for a period of several days, fecal and total coliform should be
less than 104 cells per gram 90 percent of the time and below 106 cells per
gram 100 percent of the time, and salmonella should be below detectable
levels 90 percent of the time and below 104 cells per gram 100 percent of
the time.  Consistent readings of total and fecal coliform above 105 or 106
cells per gram probably indicates poor operations as would salmonella  above
10^ or 104 cells per gram.
                                      46

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                                 References


 1.   Hoyle, Tanner & Associates, Inc.   Report on Sludge Composting at the
      Proposed Wastewater Treatment Plant,  Durham, New Hampshire.   EPA/WS
      & PCC Project No. C330161-02 Amendment No.  1.  August 25,  1976.

 2.   Urban Services Group,  Final Report -  Markets Study for Composted
      Sewage Sludge in the Metropolitan Washington Area, Metropolitan
      Washington Council of Governments. January 17, 1977.

 3.   Colacicco, D., Epstein,  E., Willson,  G. B., Parr, J.  F.,  Christensen,
      L. A.  Costs of Sludge Composting.

 4.   Joseph, J. T. Feasibility of Composting Raw Sewage Sludge by High Rate
      Suction Aeration Techniques.  EPA Solid Waste Demonstration  Grant
      S-803828-01, April 1976.

 5.   Crombie, George and Barter, Robert D.  Application and Economics of
      Forced Aeration Composting of Sewage  Sludge.

 6.   Epstein, E., Willson,  G. B., Burge, W. D.,  Mullen, D. C., and Enkiri,
      N. K.  A Forced Aeration System for Composting Wastewater Sludge.
      Jour. WPCF.  Vol. 48,  No. 4, April 1976. Page 688.

 7.   Kawata, Dr. K., Cramer,  William N., Burge,  W. D.  Composting Destroys
      Pathogens.  Water and Sewage Works, April 1977.  Page 76.

 8.   Geldreich, E. E. and Clarke, N. A.,  "The Coliform Test:  A Criterion
      for Viral Safety of Water."  Proceedings of the 13th Water Quality
      Conference, Urbana, 111., 103-113 (1971).

 9.   Hornick, R. B., et al.,  "Typhoid Fever:  Pathogenesis and Immunologic
 .     Control."  New Eng. J. of Med., 283,  686 (1970).

10.   Nccullough, N. B., and Eisele, W., "Experimental Human Salmonellosis I.
      Pathogenic!ty of Strains of S. Meleagridis  and S. Anatum Obtained from
      Spray-Dried Whole Egg."   J. Infectious Disease, 88, 278 (1951).

11.   McCullough, N. B., and Eisele, W., "Experimental Human Salmonellosis
      III.  Pathogenicity of Strains of Salmonella Newport, S.  Derby and
      S. Bareilly Obtained from Spray-Dried Whole Eggs."  J. Infectious
      Disease, 89, 209 (1951).
                                     47

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12.   McCullough, N. B., and Eisele, W. , "Experimental Human Salmonellosis
      IV.  Pathogenicity of Strains of Salmonella Pullorum Obtained from
      Spray-Dried Whole Eggs."  J. Infectious Disease, 89, 259 (1951).

13.   Kerr, R. W., and Butterfield, C. T., "Notes on the Relationship Bet-
      ween Coliforms and Enteric Pathogens."  Pub. Health Rep., 58, 589
      (1943) .

14.   Fair, G. M. , Geyer, J. C. and Okun, D. A.  Elements of Water Supply
      and Wastewater Disposal, 2nd Ed., John Wiley & Sons, New York,  1971,
      512.

15.   Mechelas, J. M.,  et al., "An Investigation into Recreational Water
      Quality."  Water Quality Data Book, Vol.  4.  EPA 18040 DAZ 04/72.
      U.S. Printing Office,  Washington, D. C. (1972).
                                    48

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                       LIST OF METRIC CONVERSIONS
English Unit
acre
bushels
cu ft
.cu yd
op
ft
in
Ib
mile
sq ft
ton (short)
Multiplier
  0.405
  0.035
 28.32
  0.765
  0.555{°F-32)
  0.3048
  2.54
  0.454
  1.61
  0.0929
  0.907
Metric Unit
 ha
 cu m
 1
 cu m
 °C
 m
 cm
 kg
 km
 sq m
 ton  (metric)
                                49

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                                 APPENDIX

                FORCED AERATION COMPOSTING AND APPLICATIONS
     Composting is the biological oxidation of organic matter by aerobic
thermophilic organisms, or anerobic, mesophilic organisms.  The forced
aeration method of composting is an aerobic, thermophilic process as pre-
sently practiced.  Aerobic conditions are maintained in the pile by forced
ventilation, compared to mechanical turning in the windrow process.  The
forced aeration method is significant because need for sludge digestion is
eliminated and raw (undigested) sludge cake can be used without causing
odor problems.  In addition, the piles remain fixed during the composting
period, higher and more uniform composting temperatures are developed and
maintained, less land is required, and, generally, more conventional and
less costly machinery is required as compared to windrow composting.  The
forced mechanical aeration allows operation personnel to effect some pro-
cess control by adjusting the aeration operating cycle.

     Raw limed dewatered wastewater sludge  (approximately 20-25 percent
solids) is mixed with a bulking agent prior to formation of the pile.  The
ratio is not necessarily fixed and, commonly, is two to three parts bulking
agent to one part sludge cake by volume.  The purpose of the bulking agent
is to increase the porosity of the sludge cake to assure aerobic conditions
during composting and to reduce the moisture content of the mix to an
acceptable level (50 to 60 percent).  Bark and wood chips have been used
successfully as bulking agents, but other materials may also be suitable.
Complete mixing of the bulking agent and sludge is essential.

     A base is prepared for the pile consisting of a perforated aeration
header and approximately 12 in of bulking agent or unscreened compost.
The base plan dimensions are the same as the bottom of the finished pile,
typically 15 to 24 ft wide and 40 to 50 ft long, although the dimensions
can be changed to match the requirements of the specific situation.  The
base is important in providing proper air distribution in the pile.

     The sludge-bulking agent mixture is piled on this base to a typical
height of 10 ft forming a triangular cross section.  The pile is capped
on all exposed surfaces with a 12 to 18 in layer of screened or unscreened
compost which insulates the active pile, limits the precipitation which
penetrates into the pile, and absorbs odors.  This pile configuration can
be constructed using commercially available front loaders and contains
approximately 50 cu yd of dewatered sludge and 150 cu yd of bulking agent
in addition to the base and cap materials.  Other size piles can be con-
structed.
                                    50

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     Additional individual piles are normally constructed as  sludge is
available or the initial pile can be "extended"  by placing a  new pile
immediately adjacent to one side of the last pile  forming a wider  continu-
ous pile.  These configurations are shown in Figure  A.

     The aeration header is attached to the suction  side  of a blower capable
of producing an air flow of 200 to 300 cu ft per minute (for  the size pile
described).  The blower discharge is piped into  a  smaller pile  of  un-
screened compost which effectively deodorizes the  gases drawn from the
composting pile.  Water condenses in the blower  suction piping  and some
means must be provided to remove this water either by careful grading of
the piping or installation of a moisture drain or  trap.

     A seven week cycle consisting of composting and curing has been used
sucessfully.  The pile is operated for the first three weeks  (or more if
necessary due to weather) with the blower providing  the forced  aeration.
Interior pile temperatures and oxygen levels should  be monitored regularly.
Oxygen levels should be in the range of 5 to 15  percent and interior temper-
atures should rise to and remain above 60° centrigrade during a major por-
tion of the composting period.  The lowest temperatures are generally near
the outside of the pile.  The blower can be operated continuously  or on
various on-off cycles during composting to maintain  optimum conditions.
Operating installations have demonstrated that pile  temperatures can be
maintained above 60° centigrade for a week or more under severe New England
winter weather conditions if proper composting techniques are used.

     Upon completion of composting, the material in  the pile  is moved to  a
stockpile for curing and storage prior to distribution.  The  curing period
is typically 4 weeks and is an added safety measure  prior to  distribution
because elevated temperatures are maintained during  curing.  In most cases
the compost is screened either prior to or after curing to control the
maximum particle size of the compost product and to  recover a portion of
the bulking agent.  The cost of the bulking agent  can be substantial there-
fore, recovery and reuse may be very important to  the overall economics.
It has been shown that wood and bark chip bulking agents can  be reused  a
number of times, however these materials do deteriorate and some passes
through the screening becoming a part of the final compost product,  so  a
portion is lost during each composting cycle.  Reportedly, 20 to  30 percent
is lost during each cycle, but this depends somewhat on the mesh  size of
the screening.

     The foregoing is only a general description of the process.   Continual
modifications and improvements are being made and it is expected that  this
process of change will continue.

     Two installations have been practicing forced aeration composting for
two years or more and are described as illustrations of the process.  The
third location has practiced forced aeration composting for a year and is
planning a new installation which should be under construction  soon.
                                     51

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          AIR IN,

                                                               DEODORIZED
                                                               EXHAUST
                                                                AIR
                            GENERAL LAYOUT
         BULKING AGENT AND
           SLUDGE MIXTURE
       COMPOST  COVER
   UNSCREENED COMPOST
  OR BULKING AGENT

      PERFORATED
        PIPE
                           15  TO 24 FT

                            CROSS SECTION
      SCREENED
      COMPOST
      (5 cu yd)

SUBSEQUENT PILES
FOR EXTENDED PILE
    METHOD
Figure A.   Typical forced aeration compost pile for 50 cu yd of
           dewatered sludge.
                                    52

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BELTSVILLE, MARYLAND

     The MES and ARS have jointly operated a demonstration and research
wastewater sludge composting facility at Beltsville for several years.
Initial work centered on windrow composting, but this process was found to
be unsuitable for composting raw wastewater sludge because of odor problems.
This led to the development of the forced aeration method in 1973.  Subse-
quent demonstrations showed that raw wastewater sludge can be composted
by this method without producing offensive odors in addition to producing
higher composting temperatures.  This method requires less space and
eliminates the requirement for regular turning of the compost as compared
to windrow composting.  Work is continuing in an effort to further improve
this method and develop additional performance data.  Approximately 350
wet tons per week of raw dewatered wastewater sludge is composted at the
10 acre Beltsville site.

     The site w.hich was previously used for windrow composting, is being
converted to an efficient layout for forced aeration composting.  Paved
composting pad areas, both covered and uncovered, are being constructed
in addition to covered storage and working areas.  It is estimated by
ARS personnel that at least 150 wet tons per day of sludge could be com-
posted on this site using the extended forced aeration method.

BANGOR, MAINE

     The City of Bangor, Maine, population  38,000 has been composting limed
raw primary sludge cake since mid 1975 using the forced aeration method as
developed by USDA.

     The City generates approximately 40 wet tons  (50 cu yd) of sludge each
week  (approximately 20 to 25 percent solids).  The sludge is dewatered and
delivered to the compost site once a week from the wastewater  treatment
plant.  A hydraulically operated, rear loading, lift and carry type
vehicle is used to haul the dewatered sludge to the compost site  in open
top containers.  The compost site is located 3 miles from the  wastewater
treatment plant and 2,000 ft from the Bangor International Airport terminal,
on approximately 66,000 sq ft of abandoned  concrete taxiway.   Shreaded bark
is used as a bulking agent.  A front end loader is used to move the bulking
agent, mix the materials, form the piles, and move the compost.

     After composting is complete, the product is  stored and  it is planned
for use by the City for applications such as land  reclamation, ornamental
plantings, parks, highway plantings, and similar soil conditioning appli-
cations.

DURHAM, NEW HAMPSHIRE

     The Town of Durham composted approximately 40 to 50 wet  tons per week
of limed raw dewatered primary sewage sludge  (approximately  20 percent
solids) from early 1975 to mid 1976 using the  forced aeration method as
developed by USDA.  The purpose of the work at Durham was to  determine that
adequate composting temperatures could be attained in a cold  northern


                                     53

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climate and to ascertain the costs of operation.  The work was funded in
part by the State of New Hampshire Department of Public Health.

     As the result of a favorable test program, forced aeration composting
is being incorporated into plans for expansion of the wastewater treatment
facility to secondary treatment.  Many of the labor intensive and critical
operations such as sludge - bulking agent mixing will be mechanized to
reduce operating costs and enhance process performance.

     Durham officials concluded that forced aeration composting produced a
safe and usable product in a cold northern climate and that the system
design being developed is cost effective compared with other disposal
methods.  These conclusions are based on results of the actual full scale
test program during 1975 and 1976 and an engineering predesign study.
                                    54

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                                  TECHNICAL REPORT DATA
                           (Please read Instructions on the reverse before completing)
i. REPORT NO.
   EPA-600/2-78-057
                             2.
                                                           3. RECIPIENT'S ACCESSION NO.
4. TITLE ANDSUBTITLE
                                                           5. REPORT DATE
   A Study  of Forced Aeration Composting of
   Wastewater Sludge
              June  1978 (Issuing Date]
            6. PERFORMING ORGANIZATION CODE
7. AUTHORIS)
   William  F.  Ettlich and
   Anne E.  Lewis
                                                           8. PERFORMING ORGANIZATION REPORT NO.
3. PERFORMING ORGANIZATION NAME AND ADDRESS
   Gulp/Wesner/Culp
   Clean Water Consultants
   P. 0. Box  40
   El Dorado  Hills, CA  95630
             10. PROGRAM ELEMENT NO.
              1BC611, AP C611B, SOS #1,
                    fl
*7
             11. CONTRACT/GRANT NO.
               68-03-2186 (Task 10)
12. SPONSORING AGENCY NAME AND ADDRESS
   Municipal  Environmental Research  Laboratory--Cin.,OH
   Office  of  Research and Development
   U. S. Environmental Protection  Agency
   Cincinnati,  Ohio 45268
             13. TYPE OF REPORT AND PERIOD COVERED
                  Final
             14. SPONSORING AGENCY CODE

               EPA/600/14
15. SUPPLEMENTARY NOTES
   Project  Officer:  Francis  L.  Evans,  III  513/684-7610
16. ABSTRACT
   The overall  study objective was to make an  independent  assessment of the  forced
   aeration wastewater sludge composting method as practiced at Beltsville,  Maryland
   and Bangor,  Maine.  A number  of  visits were made to  both sites to observe operations
   under  all weather conditions  and to gather data.  The  analyses developed  are based
   on information obtained during the site visits, information provided by various
   agencies and individuals, and independent observations  and calculations.

   Results  of the study indicate that forced aeration sludge composting can  be
   carried  out  in a satisfactory manner under nearly all  weather conditions  including
   severe New England winters.   A number of problems and  potential problems  are
   identified along with possible solutions.  Costs are very dependent on the size
   of the operation and the methods used.  Several possibilities are explored for
   reducing costs.
17.
                                KEY WORDS AND DOCUMENT ANALYSIS
                  DESCRIPTORS
                                              b.lDENTIFIERS/OPEN ENDED TERMS
                                                                           COSATI Field/Group
   Composts, Sludge, Sludge disposal,
   Sludge drying, Sludge  digestion,
   Microorganism control  (sewage),
   Aerobic processes, Distribution,
   Cost estimates, Odor control,
   Aerobic bacteria, Sewage treatment
 Wastewater sludge,
 Sludge  forced aeration,
 Compost distribution
             13B
18. DISTRIBUTION STATEMENT


  RELEASE TO PUBLIC
19. SECURITY CLASS (ThisReport)
     UNCLASSIFIED
      21. NO. OF PAGES
              63
20. SECURITY CLASS (This page)
     UNCLASSIFIED
      22. PRICE
EPA Form 2220-1 (9-73)
                                             55
                                                     U. S. GOVERNMENT PRINTING OFFICE: 1978-757-140/1340 Region No. 5-11

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