United States
         Environmental Protection
         Agency
Office of
Research and Development
Washington, DC 20460
EPA/625/6-91/031
September 1991
EPA     Handbook
         Material Recovery
         Facilities for
         Municipal Solid Waste

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                                    EPA 625/6-91/031
                                      September 1991
               HANDBOOK
     MATERIAL RECOVERY FACILITIES
       FOR MUNICIPAL SOLID WASTE
                  by

        PEER CONSULTANTS, P.C.
          Dayton, Ohio 45432
                  and

          CalRecovery,  Inc.
          Richmond, CA 94804
       Contract No.  68-03-3490
         Work Assignment 3-13
           Project Officer

            Edwin F.  Earth
 U.S.  Environmental Protection Agency
    26 W.  Martin Luther King Drive
         Cincinnati,  OH 45268
U.S.. Environmental Protection Agency
  Office of Research and Development
        Washington,  D.C. 20460
                                   Printed on Recycled Paper

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                              NOTICE

     This document is intended to assist regional,  state, and local
community  personnel,  as  well  as  individuals  or  corporations
considering  the establishment  of a  material recovery  facility
(MRF) .   This document is  not a regulation and should not be used as
such-.  The users of this handbook must  exercise their discretion in
using the  information  contained herein  as  well  as other relevant
information when evaluating MRFs.  The development and compilation
of the  guidance and information contained in this handbook has been
funded  wholly  or  in  part by  the United  States  Environmental
Protection Agency through Contract 68-03-3490 to PEER Consultants,
P.C. .
     Mention  of  trade  names  or  commercial products
constitute endorsement or recommendation for use.
does  not
                               11

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                             ABSTRACT

     The purpose of this document is to address the technical and
economic aspects of material  recovery facility  (MRF) equipment and
technology in such a manner that  the document may be of assistance
to solid waste planners and engineers at the  local community level.
This  document points  out what  technically  can  be  done,  what
material specifications  can  be achieved,  and  what the  different
manual and mechanical materials separation and recovery approaches
can cost.

     This handbook is designed for use primarily by engineering or
other technically trained personnel who  are  engaged in some aspect
of  design,  specification, purchase, or implementation  of  MRFs.
Sources  of  information   for  this  document include  the  design
engineering community,  vendors of equipment, and  various studies
funded by the U.S. EPA.   Of course,  many presently operating MRFs
also served as prime sources  of information.
                               111

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                             CONTENTS
Notice	ii
Abstract	iv
Figures	vii
Tables	viii
Acknowledgement 	 ..... x

  1  Introduction	1-1

  2  Specific Approaches to Materials Recovery  	 2-1
     2.1  Introduction	2-1
     2.2  Concept Description 	 2-1
          2.2.1   Basic MRF	2-2
          2.2.2   Variations from the Basic MRF	2-5
     2.3  Technical	2-5
          2.3.1   Waste Characterization  	 2-5
          2.3.2   Mass Balance	2-7
          2.3.3   Technology Considerations for a Basic MRF . 2-9
          2.3.4   Finished Product Specifications 	 2-9
          2.3.5   Flow Chart and Mass Balance—Low
                  Technology	2-9
          2.3.6   Flow Chart and Mass Balance—High
                  Technology—Paper Line	2-16
          2.3.7   Flow Chart and Mass Balance—High
                  Technology—Commingled Container Line .  .  2-16
          2.3.8   Flow Charts/General Comment 	  2-23
          2.3.9   Material Densities  	  2-23
          2.3.10  Fixed Equipment 	  2-25
          2.3.11  Rolling Equipment 	  2-55
          2.3.12  Human Factors 	  2-57
          2.3.13  Acceptable Waste  	  2-64
          2.3.14  Raw Material Storage  	  2-64
          2.3.15  Product Storage 	  2-66
          2.3.16  Building  	  2-66
     2.4  MRF Management	2-66
          2.4.1   Organization	2-66
          2.4.2   Operating Schedules 	  2-68
          2.4.3   Job Descriptions	2-68
          2.4.4   Health and Safety Considerations  ....  2-71
     2.5  MRF Economic Analysis	2-71
          2.5.1   Introduction	2-71
          2.5.2   Composition of Recyclables  	  2-72
          2.5.3   Capital  Costs	2-72
          2.5.4   Operating Costs	2-79
          2.5.5   Sensitivity of Capital and Operating
                  Costs	2-82
     2.6  Performance Guarantees  	   2-82
          2.6.1   Facility Availability  	   2-82
          2.6.2   Facility Capacity 	   2-82
          2.6.3   Environmental  Guarantee 	   2-83
                               v

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                       CONTENTS (Continued)
     2.7  Marketing	2-83
          2.7.1   Market Concerns for Recovered Wastepaper   2-83
          2.7.2   Market Concerns for Recovered Steel
                  Containers	2-84
          2.7.3   Market Concerns for Recovered Glass .  .   .  2-87
          2.7.4   Market Concerns for Recovered Aluminum   .  2-90

  3  General MRF Concerns 	 3-1
     3.1  Siting and Permitting Concerns  	 3-1
     3.2  Contracting Issues	3-4
          3.2.1   Contractual Arrangements  	  .3-5
          3.2.2   Flow Control	3-8

Appendix A - Glossary	 A-l
Appendix B - List of Material Grades and Specifications .   .  . B-l
Appendix C - Examples of Maintenance Procedures 	 C-l
Bibliography  	  BB-l
                               VI

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                             FIGURES
Number

 2-1
 2-2
 2-3

 2-4

 2-5

 2-6

 2-7
 2-8
 2-9
 2-10
 2-11
 2-12
 2-13
 2-14
 2-15
 2-16
 2-17
 2-18
 2-19
 2-20
 2-21
 2-22

 2-23
 2-24

 2-25
 3-1
 Flow  Chart  Source  Separated Materials  	  2-3
 Summary  Flow  Chart and Mass Balance	2-10
 Flow  Chart  and Mass Balance—Low Technology—
 Paper Line	2-13
 Flow  Chart  and Mass Balance—Low Technology—
 Commingled  Container Line  	   2-14
 Flow  Chart  and Mass Balance—High Technology—
 Paper Line	2-17
 Flow  Chart  and Mass Balance—High Technology—
 Commingled  Container Line  	   2-18
 Flow  Chart—High Technology—Ferrous Module . .  .   2-19
 Flow  Chart—High Technology—Glass Module  ....   2-21
 Flow  Chart—High Technology—Plastics Module  .  .   2-22
 Flow  Chart—High Technology—Aluminum Module  .  .   2-24
 Trough Type Belt Conveyor	2-29
 Belt  Conveyor with  Skirtboards	2-29
 Multiple Magnetic  Drum   	   2-36
 Magnetic Head Pulley	2-36
 Magnetic Belt	2-37
 Disc  Screen	2-37
 Trommel Screen  	   2-39
 Vibrating Screen   	   2-39
 Vertical Air Classifiers   	   2-41
 Typical Range of Dimensions for Can Densifiers   .   2-43
 Typical Range of Dimensions for Can Flatteners   .   2-44
 Typical Range of Dimensions for Glass Crushers
 (with Infeed Conveyor)   	  2-46
 Baler	2-46
Typical Range of Dimension for Single Ram
 Balers	2-48
Typical Range of Dimension for Two Ram Balers .   .  2-48
The Three-Phase Siting Framework  	 3-2
                              Vll

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                              TABLES


Number                                                       Page

 2.1      Example of Composition of Residential Curbside
          Recyclables	2-6
 2.2      Common Design Considerations of Low Technology
          Systems	2-11
 2.3      Common Design Considerations of High Technology
          Systems	2-12
 2.4      Factors Affecting Material Recovery Rate  ....  2-15
 2.5      Average Densities of Refuse Components  	  2-26
 2.6      Fixed Equipment Which May be Employed in a
          Materials Recovery Facility 	  2-27
 2.7      Approximate Conveyor Belt Capacities (20° Trough)
          (TPH)	2-30
 2.8      Approximate Conveyor Belt Capacities (35° Trough)
          (TPH)	2-31
 2.9      Approximate Conveyor Belt Capacities (Flat Belt)
          (TPH)	2-32
 2.10     Approximate Conveyor Belt Capacities (Flat Belt
          with 6-in. High Skirtboards) (TPH)  	  2-33
 2.11     Typical Production Rates (Ib/hr) and Horsepower
          for Aluminum Can Densifiers	2-43
 2.12     Typical Production Rates (Ib/hr) and Horsepower
          for Aluminum Can Flatteners	• .   '.  2-44
 2.13     Typical Production Rates (TPH)  and Horsepower
          for Glass Crushers	2-46
 2.14     Typical OCC Production Rates and Horsepower for
          Horizontal Balers 	  2-48
 2.15     Typical Densities and Weights (45"x30"x62")  for
          Baled Materials	2-49
 2.16     Material Recovery Efficiencies for Separating
          Equipment	  2-52
 2.17     Examples of Front-End Loader Capacities 	  2-56
 2.18     Approximate Range of Staffing Requirements for
          Material Recovery Facilities  	  2-58
 2.19     Manual Sorting Rates and Efficiencies 	  2-58
 2.20     Recommended Maximum Sorting Belt Widths 	  2-60
 2.21     Flat Belt Capacity	2-60
 2.22     Materials to be Collected for Recycling Newspaper,
          White Office Paper,  Corrugated Cardboard, Glass,
          Tin Cans,  Aluminum,  and Plastic 	  2-65
 2.23     Number of Full-Time Equivalent (FTE) Employees   .  2-67
 2.24     Operating Schedules of MRFs	^  . .   .  2-69
 2.25     Assumed Recyclables Composition 	  2-73
 2.26     Typical MRF Construction Costs ($/sq ft
          Floor Area	   .  2-73
 2.27     Typical MRF Floor Area Requirements by Throughput
          Capacity	2-74
                              Vlll

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                       TABLES  (Continued)
Number

 2.28     Estimated Construction Cost Range by Throughput
          Capacity  	
 2.29     Typical Unit Equipment Costs  	 . .
 2.30     Estimated Equipment Cost by Throughput Capacity .
 2.31     Estimated Total Capacity Cost Range by Through-
          put Capacity  	
 2.32     Typical MRF Labor Requirements  	
 2.33     Typical MRF Unit Operating and Maintenance Costs
 2.34     Estimated Annual O&M Costs by Throughput
          Capacity  	 •
 2.35     Waste Paper Recovery Figures  	 .
 2.36     U.S. Aluminum UBC Recycling Rates 	 .
 3.1      Sample Table of Contents for an RFP (To Receive,
          Process, and Market Household Recyclable
          Materials)  	
 3.2      Sample Table of Contents for a Proposal .  .   . .
2-75
2-76
2-77

2-78
2-80
2-80

2-81
2-85
2-90
 3-6
 3-9
                                IX

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                          ACKNOWLEDGEMENT

      This document was prepared in partial fulfillment of Contract
 68-03-3490,  Work Assignment  3-13  by  PEER Consultants,  P.C.,  under
 sponsorship  of the U.S.  Environmental  Protection Agency.   Edwin
 Earth of _ the  Center  for  Environmental  Research  Information,
 Cincinnati,  Ohio, was the Technical Project Manager responsible for
 the  preparation of this  document.   Acknowledgement  is given  to
 Steven J. Levy of the Office  of Solid Waste and Lynnann Hitchins of
 the  Risk Reduction Engineering Laboratory, who provided  guidance
 and  support.  Special acknowledgement is given to:

          Ms.  Darlene Snow  and  Mr.  Jack  Legler,  National  Solid
          Waste Management Association;
          Mr. James Meszaros and Mr.  Robert Davis;  Browning Ferris
          Industries;
          Mr. Jessie Buggs,  Prince Georges County,  MD, Residential
          Programs;
          Mr. Chaz Miller, the Glass Packaging Institute;
      -    Mr. Richard Kattar, New England, CRInc.;
          Mr. Bill Moore and  Mr. Dan Kemna, Waste Management,  Inc. ;
          and
          Mr. Mike McCullough, Ohio EPA,

all of whom  served as advisory committee members and/or technical
reviewers and contributors.

Participating in the development of this document were Dr. Joseph
T. Swartzbaugh and Mr. Donovan S.  Duvall  of PEER Consultants, P.C.,
and Dr.  Luis F. Diaz and Mr.  George M.  Savage of CALRecovery Inc!

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                            SECTION 1

                           INTRODUCTION

   The purpose  of this document is to  address  the technical and
economic aspects of material  recovery  facility (MRF) equipment and
technology in such a manner that the document may be of assistance
to solid waste planners and engineers at the local community level.
This  document points  out what technically  can  be  done,  what
material specifications  can  be achieved,  and what the different
manual and mechanical materials separation  and recovery approaches
can cost.

   This technology transfer document is a handbook intended for use
primarily (but not exclusively) by engineering or other technically
trained personnel who are engaged  in some aspect of specification,
purchase, or implementation of MRFs.   It should be  noted that this
handbook  offers  some  design-related  information,  but  is  not
intended to be a design guide.  For this document,  a MRF is defined
as a  central operation where  commingled and/or source separated
recyclables  are  processed  mechanically or manually.    Here,  a
separation  and/or beneficiation of recyclables prepares  them to
meet market  specifications for sale.   Sources  of information for
this document include the design engineering community, vendors of
equipment, and U.S. Environmental  Protection Agency (U.S. EPA) and
other federal agency documentation of process evaluations for MRFs.
Of  course,  many  presently  operating MRFs also served  as  prime
sources of  information.

   This document focuses primarily on equipment and methods for the
separation  and handling of separable or  already source-separated,
recyclable  constituents  in   the  typical  municipal solid  waste
stream.   For any single  recyclable constituent  within the solid
waste stream, alternative approaches are identified for separation
and recovery (namely,  manual versus  fully automated  versus some
kind  of  combined  approach utilizing  both  manual  and mechanical
methods) .    For  each  piece   of  equipment   in  any  approach,  the
document  addresses:   the  basis of design;  theory of operation;
sizing; and equipment  needs  such  as  shredders,  balers,  etc.  The
document descriptions include any limitations on materials in the
feed to  the equipment,  area  requirements,  building requirements,
possible  citing  and permitting requirements,   industrial health
concerns, and level of operator experience  and training needed for
proper  operation.    In addition,  economic  factors are discussed:
purchase  price;  utility  requirements;   maintenance  costs;  labor
costs;   auxiliary   equipment   purchase   needs;   sizing;   space

                                1-1

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 requirements;  redundancy  requirements;  and all aspects necessary
 for the  development of performance and equipment specifications.
 The key  focus  is  on the percent waste reduction (efficiency) and
 costs.  The document is intended to give guidance to the engineer
 as to what should be incorporated  into startup, implementation and
 acceptance testing  of any equipment and systems to be included in
 the MRF.

    MRFs are relatively new in the solid waste management field, but
 their popularity is fast increasing.  In the early 1980s, the first
 MRF was  established in Groton,  Connecticut.  This  facility was
 primitive  by  today's  standards  (not  full  scale).   The  Groton
 facility today is operational,  but  it does not accept any of the
 paper or plastic streams,  which are vital and integral components
 of any full-scale MRF.  Recently  104  MRFs  were identified in the
 U.S.  with about one-third operational, about half (51 percent)  in
 early  or   advanced   stages    of   planning,  11 percent   under
 construction,   and  4 MRFs  temporarily  shutdown  or  undergoing
 significant retrofitting (GAA,  1990) .

    An  obvious  question to many parties  is  the sudden  increased
 interest in the MRF as  an approach  to  processing  solid  waste
 Interest stems from:

        desire to reduce MSW going to  landfill;
        achieve this reduction by maximizing  recycling; and
        MRFs simplify generator requirements,  and thus  increase
        participation in recycling.

 The probable principal reason is that as solid waste disposal costs
 keep rising, a greater impetus develops in the favor  of recycling
 and the development of more MRFs. For example, when landfill costs
 were less than $10 per ton, recycling most of the waste stream was
 not economically attractive to the waste industry.   However, now
 with  tipping fees in some  areas approaching, or even exceeding,
 $100 per  ton,  waste managers are willing to spend more time and
 money  on  recycling.

    The appeal of MRFs seems to fall into three principal categories
 (Biocycle,  1990):

        the feedstock of most MRFs  is commingled recyclables;
        collection needs can be simplified,  and
        materials processed through MRFs  are more marketable.

 Citizens are encouraged to participate in a MRF operation, and as
 a result of this success of citizen participation, higher volumes
 of materials will be taken  from the solid waste stream.   Second
 because of the commingled nature of recyclables,  collection vehicle
 needs  can be  simplified.   Need  for  multicompartment vehicles is
 reduced; normally only two compartments are required.  Collection
times and costs can also be  reduced,  because less time is spent at

                               1-2

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the  curb  sorting  materials  or  emptying  several  containers.
Finally, most advocates believe  that  materials processed through
MRFs are more marketable.   They feel that the products of MRFs are
cleaner,  can  better  meet  industry  standards,  and  that  the
consistent volume  of material that  they  can  generate  helps  to
assure a market.

   The design of MRFs must be such that commingled recyclables can
be separated,  and the separated materials processed into marketable
commodities.   Most MRF vendors have their own basic design concept,
but they maintain the flexibility to modify their design depending
upon the  specific  requirements of the individual MRF.   In other
words, vendors can respond to the needs of  the community and try to
provide a system that will process the recyclables that are common
to that community.

   Even though many of the MRF systems are highly mechanized, there
are still many  jobs that  are best done by  humans.   For example,
nearly  all  of the  systems presently in use  hand sort  glass  by
color.   This  approach is  still  the  most  reliable way  to ensure
quality.   In  any  case,  the trade-off  between  the manual  and
mechanical MRFs is capital cost versus operating cost.  The highly
mechanical systems have a capital cost that ranges from 75 to 100
percent higher  than those for the manual  systems.   A life-cycle
cost analysis over  the operational life of the facility may show
that  the higher  operational costs  for  labor  intensive  manual
systems will become more important than the  initial higher capital
costs for mechanical  systems.  However, operating experience for
either  type  system  is  still  too limited  to allow independent
evaluation of the actual useful life of such facilities.

   The chief processing problem in any MRF  is separating the mixed
bottles and cans.  Most of the MRF systems  utilize a magnet to pull
the steel cans from the mixed materials.  Once the ferrous material
is separated it can be either shredded or baled, depending upon the
market.  The remaining fraction then includes the glass, aluminum,
and plastics.   At this point in the process,  mechanical systems can
be used to either  separate the  lighter  fraction,  aluminum and
plastics, from the glass.  The more manual systems normally utilize
workers to perform this function as well as to separate the glass
by colors.  The mechanical systems,  however, still normally use a
manual  sort  for  separating  glass  colors;  after  the glass  is
separated it can be crushed and stored for  market.  Aluminum can be
separated from the mixed materials either manually or  with aluminum
separating  equipment  such  as  eddy  current   separators.    When
plastics are accepted at  the MRF,  they  are normally separated by
type.

   While  theoretically all the materials coming into a MRF should
be recyclable,  it has been  shown  that systems  always  have some
residues.   Such residues  include contamination that is  mixed in
with the recyclables,  some nonrecoverable materials (such as broken

                               1-3

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mixed  glass  in a  commingled,  source-separated stream)  and some
materials which cannot be properly recognized by the sort mechanism
used in_the MRF.   The amount of residue depends heavily upon the
processing efficiency of the facilities,  and this is governed in
many  instances by how  well  the  community  has separated  its
recyclables,  and by what collection method is used.   For example,
if residents  persist in disposing of nonrecyclable material in the
system, then understandably the amount of residue increases.
                              1-4

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                            SECTION 2

            SPECIFIC APPROACHES TO MATERIALS RECOVERY

2.1  INTRODUCTION

     The purpose of this section is to provide the reader with a
basis for  understanding,  comparing, and  evaluating  the relative
merits of  different  approaches and solutions to  the problems of
materials recovery.  The information presented herein should be of
value to those public officials charged with review and decision-
making responsibilities as well as to those individuals responsible
for MRF planning and design.

2.2  CONCEPT DESCRIPTION

     Several approaches have been  proposed for  the recovery of
materials  from municipal wastes  over  the  past  40  years.   The
proposed schemes  range from low-technology  (i.e.,  low capacity,
relatively simple, labor-intensive,  minimum  hardware) processes to
high-technology   (i.e.,  high   capacity,   relatively _complex,
mechanical-intensive, high  capital  and operation and maintenance
costs)  concepts.     Similarly,  a  myriad  of devices   have  been
suggested  for  segregating one  or  more materials  from the waste
stream.  The decision to select one  approach versus another one is
affected by a  number of factors.   Some of these  factors include:
size;  cost;   location;  environmental   impacts;  and  economic
conditions of  the particular area.   There  are  a  large number of
conceptual designs and combinations  of equipment that could be
described, designed, and implemented.  The scope  of  this document
does  not  permit  lengthy  descriptions  of  all  possibilities.
Consequently,  the specific  approaches  and  concepts  described in
this document have been limited  to only some options.  In addition,
in order to avoid misunderstandings, definitions of important terms
used in the document are provided in Appendix A.  Descriptions of
the concepts and conditions used in the document  follow.

2.2.1  Basic MRF

     The discussion of design and operating  procedures  for MRFs is
based on a "conceptual" or  "basic" MRF.   Some variations from the
basic design are used to focus  on some  specific points.

     The  basic MRF  discussed  in this  document  is  one which is
designed, constructed, and operated  under  a few sets of  conditions.
The conditions apply to the  incoming waste  and to the  storage,

                                2-1

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processing,  and  shipping  of  the  recovered  materials.    The
conditions for each of these items are as follows:

     1.   Incoming Waste

               The  facility   receives  only   source   separated
               materials.   The  materials  are  delivered  in  two
               distinct forms.  One  stream consists  of paper and
               the other of commingled containers.

               Materials that would  be delivered  to  the facility
               in the  commingled container stream include: ferrous
               metals, aluminum,  glass,  PET,  and HDPE.

               Recyclable materials are delivered to  the facility
               via commercial  collection vehicles.

               The  facility  is  not  designed   to  accommodate
               self-haul vehicles.

     2.    Storage,  Processing,  and  Shipping

               For  each  of   the   two  incoming  fractions   of
               recyclable materials,  the facility will provide raw
               materials  storage,    means   for  separation   and
               processing,  storage   for  finished  products,   and
               means  for shipping  the finished  products in  the
               most_ appropriate  form.    A  description  of these
               conditions is presented in Figure 2-1.

          •.    The  types of finished products  from the  incoming
               paper stream include:  newspaper; mixed paper;  and
               some corrugated.

               The types of products from the commingled container
               stream  include:    ferrous  containers;   aluminum
               containers; PET bottles; HDPE containers; and glass
               jars and bottles.

              The forms and conditions in which finished products
              are  to  be  shipped   (and  thus,  the  processing
              necessary  to  produce  those  forms and to  prepare
              them for shipment)  are  dependent upon the economics
              of processing as well as upon the specifications of
              the ^markets.     Financial  viability  and  market
              requirements  are  two  major  considerations  that
              affect  the design of  a  MRF.    it  would  not  be
              financially  feasible,   for example,  to   increase
              product   quality  beyond   that  which  would   be
              necessary  to  market  the  entire  output  from  the
              facility.
                              2-2

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Currently markets do not exist for all of the materials that can be
recovered from the waste stream.  In those markets that do exist,
the market  specifications  are  varied.   Some  of the  forms  and
conditions applicable to the finished products include:

     •     Paper
               Separated by grade
               Baled (bale size  and/or  weight specified), or loose
               Dry (or may include wet)
               Clean (or contaminated or not weathered)

          Ferrous Containers
               Flattened, unflattened,  or shredded
               Labels removed (or not)
               Clean (or with limited food contamination)
          -     May or may not include bimetal
               Loose, baled, or densified into biscuit  form  with
               bale or biscuit size and/or weight specified

          Aluminum Containers
               Flattened,   shredded,   baled,   or  densified   into
               biscuit  form  with  bale  or  biscuit  size and/or
               weight specified
               Free of moisture,  dirt, steel, foil, lead, plastic,
               glass,   wood,  grease,   oil,   or  other   foreign
               substances

          PET and  HOPE  (handled  similarly)
               Baled,  granulated, or  loose
          -     Separated by  color or  type or mixed
               With or without caps

          Glass
               Separated by color and/or mixed
               Size of cullet (maximum  and/or minimum) specified
              Nature  and amount of  allowable  contamination   if
              any, specified

    •     General
              Available markets  for secondary materials typically
              specify the  means of packaging and shipping  each
              product.  The specifications depend upon location
              and end-use.  The  specifications often include the
              following:
              o
              o
              o
              o
              o
Skids or pallets
Bundles, bins, boxes, cartons, or drums
Trailer loads
Roll-offs
Rail cars
                              2-4

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2.2.2  Variations from the Basic MRF

     In the text to follow, references and comments will be made to
designs of MRFs which vary from the  "basic" MRF.  The comments are
made because there are some facilities that have been designed in
that manner.   In addition, the current climate  in  the  industry
points in those directions.  These variations include:

     1.   The facility receives only source separated materials in
          a single incoming waste stream.

     2.   The  facility  also  receives  other  source  separated
          materials  such  as  yard  waste,   wood  waste,  tires,
          corrugated,  mixed metals,  used  motor  oil,   lead  and
          batteries,   used clothing, appliances,  other  plastics,
          etc.

     3.   The facility receives mixed municipal solid waste (MSW)
          in addition to source separated materials.

     4.   The facility receives only mixed MSW.

     5.   In  addition to receiving recyclables  and/or mixed MSW
          from commercial haulers, the  facility receives mixed MSW
          from self-haul vehicles.

     6.   In addition to the recovery of  recyclables, the facility
          produces a refuse derived fuel (RDF).

     7.   In addition to the recovery of  recyclables, the facility
          prepares a compostable feedstock.

2.3  TECHNICAL

2.3.1  Waste Characterization

     In order  to properly design a MRF  it  is advisable  (in some
states necessary to comply with legislation), among other tasks, to
perform   an   analysis  of  the  waste   stream,   i.e.,   a  waste
characterization study, so that the variety and relative quantities
of  incoming materials can be identified and  determined.   Actual
field measurements are the preferred method  of waste analysis.  An
example of the composition of residential curbside recyclables is
presented in Table 2.1.  These  relative quantities are influenced,
for each community,  by various factors including:

     1.   State "bottle bills" which offer a  financial  incentive to
          the  consumer  to  return  the  container  (metal,  glass,
          and/or  plastic)  to  the  seller  thereby reducing  the
          quantity of the item(s) from the incoming waste stream.
                               2-5

-------
    TABLE 2.1.  EXAMPLE OF COMPOSITION OF RESIDENTIAL
                CURBSIDE RECYCLABLES*
             Material
% by weight
  Newspaper

  Mixed Paper

    Total  Paper

  Glass Bottles
    Clear
    Green
    Brown

  Tin Cans

  Aluminum Cans

  Plastic  Containers
    PET
    HOPE

    Total Commingled Containers

    TOTAL
    33

    41

    74



    11
     4
     4

     4

     1



     1
     1

    26

   100
* Not to be considered as either average or typical
2.   Community demographics which, as a result of its urban,
     suburban or rural nature, income level, reading habits,
     residential/commercial/industrial mix, and other factors
     increase or decrease the relative quantity of any item(s)
     in the incoming waste stream.

3.   Significant variations  in the relative  quantity  of an
     item(s) in  the  waste  stream may occur  due  to seasonal
     influences  (beverage  containers  in  resort areas,  for
     example).     In  addition,   changes  in  population,  as
     experienced at seasonal resort areas,  may have a marked
     consequence on the amounts and types of wastes generated.

4.   Community recycling education programs.
                          2-6

-------
     5.   Community mandated and enforced recycling programs versus
          voluntary recycling programs.

     6.   Relative  ease  (or  difficulty)  of  participating  in  a
          curbside recycling program.

     7.   Tipping  fee  differentials  between  those at  disposal
          facilities  and  at  a MRF  and/or the  banning of  some
          components  (e.g.,  tires,  yard  waste)  from  disposal
          facilities may bias the composition of the incoming waste
          stream at those facilities.

2.3.2  Mass Balance

2.3.2.1  Introduction and Preliminary Considerations—
     In addition  to determining the relative quantities  of the
various components in  the incoming  waste streams  in order  to
provide for  the storage,   separating,  and  processing of the raw
materials  as  well  as  for  the  handling of  residue and for the
storage and  shipping of  finished  products,  it  is  necessary  to
determine the anticipated amounts of each of these components.
The  process  by  which  this is  accomplished   is  called a  "mass
balance" analysis.  A proper mass balance  analysis  considers the
nature of the incoming waste streams, the level of technology to be
employed in the separation and processing of materials, the market
specifications for the end products,  the economic  justification for
separating and processing  materials,  and the legislated or project
designated waste diversion levels which must be met.  An important
factor to consider before  beginning  the mass balance analysis and
the  subsequent sizing  of  the MRF  and its  subsystems,   is  the
anticipated total tonnage  which the facility will  be  called upon to
handle.  It is  imperative that this total be identified and defined
as  accurately  as  possible.    Lacking  such   identification  and
definition, it is highly improbable  that the facility will perform
as designed.

Example:   A waste characterization  study and  landfill  records
indicate  that  a   community currently  generates 46,500  TPY  of
residential recyclables.  Also, through the use of pilot programs
and  or knowledge  of  experiences in  similar  communities,   it  is
estimated that 70% of the households may be  expected to participate
in a curbside collection program, then:

               46,500    TPY residential recyclables generated
               x   0.7    household participation rate
               32,500    TPY   maximum   available   for   curbside
                         collection
                               2-7

-------
 However,  it is also realized that within each participating average
 household,  only  80% of  the possible  recyclable materials  will
 actually  be placed at curbside for collection,  then:
                32,500
                x  0.8
                26,000
TPY maximum available
household internal participation rate
TPY collected at  curbside  and delivered
to facility.
     A MRF may be planned to operate 52 weeks per year,  5 days  per
week, or 260 days per year.  When a holiday falls on a weekday that
day may be made  up  on the weekend, then:
           26,000  TPY
           260  days/yr
     100 TPD collected at curbside and
     delivered to MRF.
Care must  be taken that anticipated growth in the population and
the probable corresponding change in the waste stream quantities
are allowed for.  This  does not mean that  the  facility must be
built to deal with the waste stream 20 years  from  now, but  it does
suggest that some planning needs to be carried out for that future
requirement.  Scheduled legislated waste diversion rates  also have
a bearing  on facility sizing.

     If the facility is to  be  properly  sized,  then the facility
capacity must be defined for the tipping floor as well as for the
processing  lines (schedule  for receiving  may be different from
processing).   In addition, the intended number of hours per day
(e.g., 8,12,16) and days per week  (e.g., 5,6,7) for receiving and
processing waste must be defined.  Further,  the size of the product
areas should reflect the  frequencies  of the shipping schedules.
Also,  the peak throughput  capacity of the facility must be set to
compensate  for surges  in  throughput  experienced  after special
events,  long weekends, major holidays, etc.

     From   a  purely   economic  standpoint,   it   is   generally
advantageous to utilize a  facility as continuously as possible at
its design capacity.   However,  there are  considerations  which
dictate that the facility  be operated  less than 24 hours per day
and/or 7 days per week,  including:

          traffic to and from the facility;
     *     noise;
     •     time allocated for preventive maintenance;
          loss of efficiency on  second  and third shifts (if normal
          operation depends upon two or three  shifts, there is less
          opportunity to make up for the inevitable down time) ; and
          substantial changes in waste deliveries  during the year
          (e.g., at resort areas).
                               2-8

-------
2.3.2.2  Process Flow Chart and Mass Balance—
     For the purpose  of  example,  it is assumed that the facility
will receive 100 TPD of paper  and  commingled recyclable containers
in the proportions according to Table 2.1.  The overall flows and
mass  balance  may  be  represented  on  a  summary  flow chart  as
illustrated in  Figure  2-2.  A 90% recovery rate has been assumed
which results in 10 TPD of residue to be landfilled.  The designer
should  realize  that  the  greater the   separation  of  material
categories  that occurs  at  the source,  the higher  the probable
recovery rate of those recyclables at the MRF.

2.3.3  Technology Considerations  for a Basic MRF

     The separation and processing steps required or desired at a
MRF are influenced by market requirements, by the characteristics
of the feedstock, and by  the economics associated with separation,
processing,  and transportation.   Additionally,  in  geographical
areas where labor wages are historically low and unemployment high,
there is greater reason  to  favor  a labor intensive approach than
there is in those areas where labor is scarce and labor wages high.
The total  quantity  of materials  and the  relative percentages of
material grades or categories  will have an effect upon the methods
employed for recovery and processing,  and most certainly upon the
equipment selected to recover and process the various materials.

     Tables 2.2  and 2.3 address  some  of the  more  common design
considerations   of   low-  and  high-technology   systems.     The
combinations of  low and high technologies  are virtually without
end.

2.3.4  Finished Product Specifications

     A select list of grades and definitions adapted from the Scrap
Specifications Circular  1990  as issued by the Institute of Scrap
Recycling Industries Inc. (ISRI)  is presented in Appendix B.  The
material in Appendix B provides specifications  for  tin and aluminum
cans.   Finally, Appendix  B  presents  examples  of actual  buyer
specifications for various recyclable materials.

2.3.5   Flow Chart and Mass Balance—Low Technology

     Using  the  proportions of  recyclable materials  as  shown  in
Table 2.1,  the flow chart and mass balance for the paper line are
shown in Figure  2-3.   Similarly,  Figure 2-4 is a  flow chart and
mass balance for the commingled  container  line.  With reference to
either of these two  figures the reader will note that more or fewer
separations may take place at  the  sorting  station.  In the case of
the paper line,  Figure 2-3, it  is possible that  the  only product
desired is  "mixed  paper" in which  case  it is only  necessary  to
remove whatever material is considered to be contaminating to the
product.  Or,  as markets develop or change, it may prove to be of
value to separate corrugated,  office paper, or mixed paper

                               2-9

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TABLE  2.2.   COMMON DESIGN CONSIDERATION OF  LOW TECHNOLOGY SYSTEMS
Material
Paper
Commingled
Containers
Basic
Feedstock
Mixed wet &
dry paper,
including
newsprint,
old corrugated
containers
(OCC), high-
grades, books,
magazines, &
contaminants
Tin, bimetal, &
aluminum cans,
plastic, & glass
containers, &
contaminants
Tipping
Floor
Handpick
OCC&
contaminants
Handpick
contaminants
Infeed
Conveyor
Handpick
OCC&
contaminants
Handpick
contaminants;
magnetic
separator for
ferrous
Sorting
Conveyor
(or room)
Handpick
OCC,
magazines,
high-grades,
mixed paper,
etc.
Handpick
plastic,
aluminum,
contaminants
Interim
Storage
In piles on
processing
floor or in
bins
In piles, bins,
or containers
Preparation
for Shipping
Ship loose, as
is, or baled
Ship loose,
as is
Finished
Product
Storage
In piles on
processing
floor, in bins,
or compacted
or baled in
transport
vehicles
In piles, bins,
containers, or
transport
vehicles
                                  2-11

-------
TABLE 2.3.  COMMON DESIGN CONSIDERATIONS OF HIGH TECHNOLOGY SYSTEMS
U»'.ttU
pjp«
tfaillttt
CommbgVxl
ConU'ntrs
IMitttl
Ferrous
(Binwul)
Petrous
(Til fens)
MaiirUI
Aluminum
Material
Ptajsc(PET)
Ibtiriil
PtiSX:
POPE)
Mjieriit
GUss
Basic
Feedstock
Mixed wot& dry
papor. including
novrtpal, old
corrugated con-
UinefstOCq,high
grades, books.
magazines &
contaminants
Btste
Feedstock
Tn. bimetal, &
aluminum cans.
plastic and gbss
containers, &
contaminants
Sort
Mania! separation
ol tin cans and
birwu! (7 required)
Manual separatnn
ol (in cam and
b'nwul {I required)
Septraie
Eddy current
apparatus
separates
alurnintjm tram
plane
Sort
Manual son ol
PET, HOPE, other
Sort
Manual sort ol
PET. HOPS, othaf
Sort
Tipping
Floor or
Sptclal Station
HandpkfcOCC
& conuminams
assisted by a
grapploUor
Iron-end loader
Tipping Floor
or Sptclal
SUilon
Handpfck
conuminants
Bait
Vfthauto-tio
babr
With aixo-tio
bater
Flattin
Wihcan
llattener
Interim
Storage
In overhead
hoppers
Interim
Storage
In overhead
hoppers

Optical automatic son or hand sort by
color
lnle«d Trommel
Conveyor
Grapple ol front- Separates
end loader oversize OCC
S/or newspaper
from mixed
paper
Infeed Conveyor
Handp'ck contaminants; magnetic
separator lor ferrous
Biscuit Shred
With can
densferand
palletize
With can With can
denslierand shredder
paEetize
Store Bale
Pneumat'eaBy With auto-tie
convey to baler
outside trans-
pon vehicte
Perforate
Drop from overhead hopper or
pneumaticafty convey to perforator
Granulate
Drop from overhead hopper or
pneumatically convey to granulator
Crush
To meet market specifications
Sorting Interim Preparation Finished
Conveyor Storage for Shipping Product
(or room) Storage
Handpkk Accumulated in Auto-tie baler In slacks or
remaining OCC, bins or bunkers bales on
magazines, high- before being processing floor
grade. & mixed selectively or stacked in
paper, etc. conveyed to transport vehicle
baler
Screen Traveling Chain Curtain
Broken glass recovered as undersized Separate aluminum and plastic from
materials glass
Air Classify Store
In stacks on processing floor,
outdoors, or in a transport vehicle
To remove Convey shredded ca ns u outside
labels transport vehicle, or bales or biscuits
in stacks on processing floor,
outdoors, or in a transport vehicle
Store Biscuit Store
In bales on Compress 'm a In stacks on the processing floor or
processing floor densifier and outdoors or in a transport vehicle
or outdoors palletize
Bale Store
Mechanically or pneumatically from In stacks or bales on processing Ikwr
perforator to auto-tie baler or outdoors in transport vehicles
Bale Store
Mechanically or pneumatically convey Granulated in gaylords on processing
from hopper to auto-tie baler floor before loading into transport
vehicle, baled in stacks on processing
floor or outdoors in transport vehicles
Upgrade Store
Remove paper labels, metal (ids, & In bunkers lor loading by front-end
other contaminants by trammel and/or loader, or in overhead bins for
air classifier selectively conveying to transport
vehicles
                                2-12

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products.   The system  can be designed to accommodate such  changes
with  minimal  capital expenditure.

       In  the case  of  the commingled container  line,  Figure  2-4,  it
is also  possible  to  increase or  decrease  the  number of material
categories  separated from  the incoming  stream.  For  example,  glass
can be sorted  by  color,  if warranted; or tin  cans, if no market  is
available,  are permitted  to  join the residue to  be  landfilled.In
each  case  depicted  in  Figures  2-2  through  2-4,  a  90%  material
recovery rate  has been  assumed.    In actual  practice  there are many
factors  which have an  influence  on  this recovery rate.    Some  of
these factors  are  listed  in  Table  2.4.
         TABLE  2.4,
FACTORS  AFFECTING MATERIAL RECOVERY RATE
 Factor
                                   Explanation
 Market Specifications
          "Loose" (i.e., unconstrained) specifications potentially
          increase recovery rates over those recovery rates that are
          attainable in the case of "tight" (i.e., constrained)
          specifications
 Contamination of
 Incoming Materials
          This factor is closely related to that of market specifications
          in that some markets will accept products which other markets
          consider as unacceptable because of contamination
 Glass Breakage
          This factor applies to glass containers and it is influenced by
          the manner in which the containers are set out, collected,
          transported,  sorted, and handled at the Facility. Broken glass
          is more difficult to sort than unbroken glass
 Relative Quantities per
 Sorter
          Over a given period of time,  the greater the number of units of
          any given recyclable a sorter must separate from the waste
          stream, the lower the recovery rate.  Conversely,  recovery can
          be increased by increasing the number of sorters utilized
 Equipment Design
          Proper design of conveyors and separation equipment for the
          types and quantities of materials handled, directly affects
          recovery rates.  For example, an excessive bed depth of
          commingled containers on a conveyor can substantially limit the
          manual or automatic recovery of any given material
 Human Factors
                                   Providing a clean, well-lit, and pleasant environment  in which
                                   to work with particular attention to worker training,  safety,
                                   health, and comfort will tend to increase recovery rates
 Fictitious Weights
          Most MRFs are now equipped with a truck scale and scale house.
          Additionally, values for tare weights for regular haul vehicles
          are either in the scale's computer data base or they are
          determined after tipping.  Care must be taken, particularly
          during periods of inclement weather, that the weight of an
          incoming load does not  include an inordinate amount of free
          water from a recent rain or snowstorm which would inaccurately
          represent the weights of incoming materials.
                                         2-15

-------
 2.3.6  Flow Chart and Mass Balance—High Technology—Paper Line

      Using the  proportions  of recyclable  materials  as shown  in
 Table 2.1, the flow chart and mass balance for the paper line are
 shown^ in  Figure 2-5.   With  reference  to this  flow chart,  the
 incoming paper is conveyed to a trommel  (a rotating cylindrical
 screening device) so designed that  large  material  (newspaper and
 corrugated)  will pass through the cylinder (oversize  material,  or
 "overs")  while small material (mixed paper) will  fall through the
 screen  openings  as  undersized  material  ("unders").    Provision
 should be made at the trommel inlet to manually divert extra-large
 pieces of corrugated which may jam the system.  It should be noted
 that the trommel may also be designed to remove grit and gravel and
 other components smaller than mixed paper that would contaminate
 the  end  product.

      At  sorting station #1, unacceptable materials are removed for
 landfilling.  In addition, corrugated and mixed paper are separated
 from the  newspaper  stream.    The trommel  "unders"  (i.e.,  mixed
 paper)  are  conveyed to  sorting  station #2  where  unacceptable
 materials  are  removed for landfilling.  The remaining paper joins
 the  corrugated removed  from sorting station  #1.   Newspaper  and
 mixed paper are collected separately and  accumulated in individual
 bins.  Each paper category is separately processed through an auto-
 tie  baler  as conditions warrant for  shipment  to markets.

      As  a  variant to this scheme, the trommel as well as  sorting
 station #2 could be eliminated.  This option,  of course,  would put
 a greater burden on the manual separation effort at sortinq  station
 #1.

 2.3.7  Flow Chart and Mass Balance—High Technology—Commingled
       Container  Line

      Continuing  with the  example,  and using  the proportions of
 recyclable materials as shown in Table 2.1, the flow chart and mass
 balance for the commingled container line  are  shown  in Figure 2-6.
 With  _reference  to  this  flow chart,  the   incoming commingled
 containers are introduced to  the processing line on a common infeed
 conveyor.  For the purposes of describing  the  processes as  well as
 to provide a modular system concept,  the commingled  container line
 is presented as consisting of four basic modules.   They are:

          ferrous module
      •    glass module
      •    plastics module, and
      •    aluminum module

 2.3.7.1  Flow Chart—High Technology—Ferrous Module—
     Flow chart,  Figure 2-7,  is an enlarged view of that portion of
Figure 2-6  which pertains  to the  separation and  processing of
ferrous material.  All commingled containers are conveyed to a

                               2-16

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magnetic  separator  whose function  is  to  extract  all  ferrous
materials from the rest  of the  commingled container  stream.   The
efficiency with which this task is  accomplished is a function of
the  design  of  the  magnetic separator,  the  bed depth  of  the
materials subjected  to  the  magnetic field,  the  ratio  of  ferrous
containers  to  other materials  and  the  proportion of  ferrous
containers which are filled or partially filled with food, liquid
or other substances.

     Once separated  from the  other  containers  and depending upon
the markets,  the  ferrous containers  are manually sorted  (sorting
station #1)  into  two streams, i.e.,  bimetal  and tin.  Residue is
collected and transported to landfill.  Bimetal containers may be
flattened, baled, or densified into  biscuit form.   Tin cans may be
flattened or shredded and introduced to'an air classifier for the
removal of labels loosened by the flattening,  or shredding process.
Alternatively, tin cans may be flattened, baled or densified with
or without bimetal cans.   Ferrous cans  that are not removed by the
magnetic  separator  from the  commingled  containers stream  are
conveyed to a sorting station where manual separation takes place.
The cans removed manually are returned, by means of  conveyors, to
join the ferrous  removed by the magnetic separator.

2.3.7.2   Flow Chart—High Technology—Glass Module—
     Flow chart, Figure 2-8,  is an enlarged view of that portion of
Figure  2-6  which pertains  to  the  separation  and processing of
glass.  After magnetic  separation of ferrous from the commingled
container stream, the remaining containers pass over a screen which
enables much  of  the  broken glass to  be removed as "unders."  The
"overs" enter a  traveling chain curtain which  separates plastic and
aluminum  containers  from  the  glass  containers.  _  The  glass
containers  are  then  conveyed  to   a   sorting   station.    Glass
containers are hand sorted by color with each  color passing through
a glass crusher.   Depending upon market specifications, each cullet
stream may be introduced to  a small  trommel  for removal of paper
labels and caps.  The mechanical removal of labels and caps may be
further  assisted by pneumatic  means.   The  "unders"  from  the
screening operation  join  the mixed glass from the  sorting station
and are processed in the same manner  as  are the various  colored
glass  containers.   Residues from  the  sorting  station  and  the
trommels are  collected and transported to landfill.

2.3.7.3. Flow Chart—High Technology—Plastics Module—
     The  flow chart,  Figure 2-9,  is  an  enlarged  view  of  that
portion  of  Figure  2-6   which  pertains  to  the  separation  and
processing of plastics.   After magnetic separation of ferrous and
the removal  of  broken glass by  the  screen,  plastic  and aluminum
containers are  separated from the glass containers by means of a
traveling chain  curtain.  An eddy current device is  then  used to
eject  aluminum  cans  from the  plastic/aluminum  substream.   The
plastic containers are conveyed to a sorting station where PET is
hand separated from HOPE. Trace plastics entrained with  the glass

                               2-20

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 substream from the air classifier or  traveling  chain curtain are
 hand separated at the glass sorting station and transferred to the
 plastics sorting station for PET/HDPE separation.

      PET containers are  collected,  perforated  and baled.   HOPE
 containers can be granulated.  The plastic granules are loaded into
 gaylords for shipment to market.  Alternatively, HOPE containers
 can be  baled  instead of  granulated.    Residue  is  collected  and
 transported to landfill.

 2.3.7.4   Flow  Chart—High  Technology—Aluminum Module—
      The flow  chart,  Figure 2-10, is an enlarged  view of  that
 portion   of  Figure  2-6 which  pertains to  the  separation  and
 processing of  aluminum cans.   After  separation of aluminum  cans
 from plastic containers by the eddy current device which employs an
 electromagnetic field to  repel nonferrous metals,  the cans  are
 flattened and  pneumatically  conveyed  to  a  transport trailer.
 Alternatively,  the cans may be baled or densified into biscuit form
 to  meet  market specifications.  Trace aluminum which may  have
 escaped  separation  from the plastics by the eddy  current device is
 routed  from the  plastics  sorting station to  the can  flattener
 baler, or densifier as applicable.                              '

 2.3.8  Flow Charts/General Comment

     With regard to the flow charts   illustrated in  Figures  2-3
 through 2-10 for low and high technology systems,  the reader should
 recognize that there  are  almost  limitless  combinations   and
 modifications  of  the systems  presented.   For example, Figure  2-6
 includes  a traveling chain  curtain  (or other automatic sorting
 device) to sort glass from the  rest of the waste stream.  If this
 operation did not exist,  then the screen "overs" would  be directed
 to  the  eddy  current  device  for aluminum  extraction  with   the
 remainder directed  to  a sorting  station which would  combine  the
 activities described as taking place at sorting stations #2 and  #3.

 2.3.9  Material Densities

    _ In order to properly size a MRF,  and to select or design the
 equipment used  therein, it is  necessary to  have  knowledge  of the
densities  associated  with  the  various materials  as  received
handled,  processed, and  stored.   All density values are the result
of  dividing the  weight of  the  material  by  its  volume.    The
differences arise due to the  forms in which the material is found.

     Material Density Definitions:

               Bulk Density:   Weight  of material divided  by  the
               volume  of that  portion  of  a  container which  is
               filled with  the material
                              2-23

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                True  Density:    Weight  of  the material  in  its
                natural  form  (e.g.,   glass,  rather  than  glass
                bottles)  divided by its volume.
                Compressed Density:  Weight of material divided by
                its volume during or after having  been exposed to
                compressive forces  in a confined space.  Cellulosic
                materials can be  compressed to densities as high as
                75 Ib/cu  ft.

 Densities of several materials  received, handled,  processed,  and
 stored at MRFs are listed in Table 2.5.

 2.3.10  Fixed Equipment

      The purpose of this subsection is  to  provide  guidance to  the
 reader who is involved in the review and selection process of fixed
 equipment as employed in a MRF.

 2.3.10.1  Fixed Equipment Commonly Present in a MRF—
      A comprehensive list of various types of fixed equipment which
 may be included in a  MRF is  presented  in Table  2.6.

 2.3.10.2  Fixed Equipment Descriptions—
      The following equipment descriptions are provided to give  the
 reader a brief overview  of machinery commonly employed  in a MRF.
 Since new special  purpose machines continue to  be developed  to
 serve this growing industry, the  list  should  not be regarded  as
 all-inclusive.      The   facility   planner/designer   should   be
 particularly cautious in  placing  reliance upon unproven technology.

      In the  review and  selection  process  of individual items  of
 fixed equipment, it should be recognized that these items must  not
 only  compatibly interrelate  with one another,  but also with  the
 various collection vehicles which deliver the incoming materials as
 well  as  in-plant  rolling equipment  and transport  vehicles  for
 shipping  the final products.

      2.3.10.2.1  Material handling  equipment  (conveyors)—the most
 common  piece of equipment for handling  materials  in a MRF is the
 conveyor.    There  are  several  types  of  conveyors  available.
 Selection of the correct  types of conveyors in a  MRF must take into
 consideration   a   number  of interrelated  factors.    Complete
 engineering  data  are available for  many  types   of  conveyors;
 consequently, their performance  can be  accurately predicted when
they   are  used   for   handling  materials   having  well-known
characteristics.  However, if the material characteristics are not
well-known, even the best designed conveyor will  not perform well.
                              2-25

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   TABLE 2.5.    AVERAGE  DENSITIES OF REFUSE  COMPONENTS
        Component
 Density
Refuse Densities

    Loose
    After dumping from compactor truck
    In compactor truck
    In landfill
    Shredded
    Baled in paper baler

Bulk Densities

    OCC
    Aluminum cans
    Plastic containers ,
    Miscellaneous paper
    Garden waste
    Newspaper
    Rubber
    Glass bottles
    Food
    Tin cans

True Densities

    Wood
    Cardboard
    Paper
    Glass
    Aluminum
    Steel
    Polypropylene
    Polyethylene
    Polystyrene
    ABS
    Acrylic
    Polyvinylchloride (PVC)

Resource Recovery Plant Products

    dRDF
    Aluminum scrap
    Ferrous  scrap
    Crushed glass
    Powdered RDF (Eco-Fuel)
    Flattened aluminum cans
    Flattened ferrous cans
   lb/ydj

 100-200
 350-400
 500-700
 500-900
 600-900
800-1200

    Ib/ft3

    1.87
    2.36
    2.37
    3.81
    4.45
    6.19
   14.90
   18.45
   23.04
    4.90

    Ib/ft3

      37
      43
   44-72
     156
     168
     480
      56
      59
      65
      64
      74
      78

    Ib/ft3

      39
      15
      25
      85
      27
       9
      31
                                   2-26

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TABLE  2.6.
FIXED  EQUIPMENT  WHICH MAY BE EMPLOYED  IN
A  MATERIALS RECOVERY FACILITY
         Material Handling Equipment
             Belt Conveyor
             Screw Conveyor
             Apron Conveyor
             Bucket Elevator
             Drag Conveyor
             Pneumatic Conveyor
             Vibrating Conveyor

         Separating Equipment
             Magnetic Separator
             Eddy Current Device (aluminum separator)
             Disc Screen
             Trommel Screen
             Vibrating Screen
             Oscillating Screen
             Traveling Chain Curtain
             Air Classifier

         Size Reduction Equipment
             Can Shredder
             Can Densifier/Biscuiter
             Can Flattener
             Glass Crusher
             Plastics Granulator
             Plastics Perforator
             Baler

         Environmental Equipment
             Dust Collection System
             Noise Suppression Devices
             Odor Control System
             Heating, Ventilating,  & Air Conditioning (HVAC)

         Other Equipment
             Fixed Storage Bin
             Floor Scale for Pallet or Bin Loads
            Truck Scale
             Belt Scale
                              2-27

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Some  of the most important  factors  to  be considered in conveyor
selection  include:

      •     capacity;
      •     length  of travel;
           lift;
      •     characteristics of the material; and
           cost.

      The most common types of conveyors used in  a MRF  are the belt
conveyor,  the  apron conveyor,  and  the screw conveyor.   A short
description of each follows.

      Belt  Conveyor

      In  a  MRF,  the belt  conveyor is employed  in several forms.
Some  of these forms include:

Trough Type:  In  general,  the trough type belt conveyor will use
troughing  idler  rolls  which cause the  conveyor belt to  form a
concave contour with its sides  sloping at 20°,  35°, or 45° with a
horizontal  plane   (see  Figure  2-11).    The  purpose  of  this
cross-sectional  concavity is  to retain  free  flowing  materials
(e.g.,  aluminum  cans,  bottles,  crushed  glass,  etc.),   and  to
minimize  or prevent  spillage.   In order  to   further  minimize
spillage problems, skirt boards (see Figure 2-12) are often  used at
belt  transfer points.

      The   Conveyor  Equipment  Manufacturers  Association  (CEMA)
provides a design handbook for belt  conveyors.   Tables 2.7  and 2.8
have  been  adapted from information published by the CEMA for some
specific materials generally handled in a MRF.

      The designer is referred to the most recent  issue  of ASME/ANSI
B20.1, Safety Standard  for  Conveyors and Related Equipment,  for
information and guidance in the design, construction, installation,
operation, and maintenance of conveyors  and related  equipment.  In
addition to general safety standards applicable to all  conveyors
and related equipment,  Section 6.1 of the Standard is  specifically
applicable to belt conveyors.

Plat Belt Type:   Most flat belt conveyors employed In  a MRF are of
the "slider belt"  design in which the conveyor belt is  backed up by
and slides on a  steel  supporting  surface  rather  than  on idler
rolls.  Flat belt conveyors are popularly utilized in the sorting
process  at a MRF  for they  permit  easy  access to the  material
carried on the  belt.    When  a flat  belt  conveyor  is used in  an
inclined position,  it  is  often supplied with  cleats and skirt
boards  for the  full  length  of the  conveyor  in  order to  more
positively convey the materials and prevent spillage.   Tables 2.9
and 2.10 have been adapted from belt capacity tables published by
the CEMA for some specific materials generally handled in a MRF.

                               2-28

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                 Belt
   Figure  2-11.  Trough type belt conveyor.
                           Skirtboards
                        Bolted Adjustable
                         Rubber Edging
                       Belt
Figure  2-12.
Belt conveyor with  skirtboards.

       2-29

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        TABLE  2.7.    APPROXIMATE CONVEYOR BELT  CAPACITIES
                       (20°  TROUGH)1'6  (TPH)
Belt Width
Component3
Glass Bottles4
Plastic Bottles4
Aluminum Cans4
News5
OCC5
Loose Refuse5
Refuse from Compactor Truck5
EXAMPLE: To find capacity at
18
6.0
0.8
0.8
3.9
1.2
3.5
8.7
other belt speeds:
24
11.6
1.5
1.5
7.5
2.2
6.7
16.6
New belt
36
28.3
3.7
3.7
18.1
5.3
16.0
40.0
speed =
(Inches)2
48
52.2
6.8
6.8
33.3
9.8
29.4
73.6
20 FPM;
60
83.4
10.8
10.8
53.1
15.6
46.9
117.2
Plastic
72
121.8
15.8
15.8
77.5
22.8
68.4
171.0
Bottles,
36 in. belt width; TPH = 20 FPM/100 FPM x 3.7 TPH - 0.7 TPH
'Conveyor Speed = 100 FPM
2Edge Distance (inches) = 0.055 x belt width + 0.9. Three equal idler roll lengths
3Densities as per Table 2-5
"Surcharge Angle = 5°
Surcharge Angle = 30°
6Based on capacities published in CEMA "Belt Conveyors for Bulk Materials"
                                     2-30

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         TABLE 2.8.   APPROXIMATE CONVEYOR  BELT CAPACITIES
                         (35°  TROUGH)1-6  (TPH)
Belt Width (Inches)2
Component3
Glass Bottles4
Plastic Bottles4
Aluminum Cans4
News5
OCC5
Loose Refuse5
Refuse from Compactor Truck5
EXAMPLE: To find caoacitv at other belt sr
18 24
8.9 17.2
1.2 2.2
1 .2 2.2
4.7 9.0
1.4 2.6
4.1 7.9
10.4 19.8
needs' Nfiw belt q
36 48 60 72
41.7 77.0 122.9 179.4
5.4 10.0 16.0 23.3
5.4 10.0 16.0 23.3
21.6 39.7 66.3 92.2
6.3 11.7 19.5 27.1
19.0 35.0 58.5 81.3
47.6 87.5 146.2 203.3
nppd — OH PPM- PlaQtir- RrvHIao
36 in. belt width; TPH = 20 FPM/100 FPMx5.4TPH = 1.1 TPH
1Conveyor Speed = 100 FPM
2Edge Distance (inches) = 0.055 x belt width + 0.9. Three equal idler roll lengths
Densities as per Table 2-5
Surcharge Angle - 5°
Surcharge Angle = 30°
6Based on capacities published in CEMA "Belt Conveyors for Bulk Materials"
                                      2-31

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         TABLE 2.9.   APPROXIMATE  CONVEYOR BELT  CAPACITIES
                        (FLAT BELT)1'6  (TPH)
Belt Width
Component3
Glass Bottles4
Plastic Bottles4
Aluminum Cans4
News5
OCCS
Loose Refuse5
Refuse from Compactor Truck5
EXAMPLE: To find capacity at
18
1.1
0.1
0.1
2.4
0.7
2.1
5.3
other belt speeds:
24
2.2
0.3
0.3
4.6
1.3
4.0
10.0
New belt
36
5.1
0.7
0.7
10.9
3.2
9.6
24.0
speed =
(Inches)2
48
9.4
1.2
1.2
19.9
5.9
17.6
43.9
20 FPM;
60
14.9
1.9
1.9
31.6
9.3
27.9
69.8
Plastic
72
21.8
2.8
2.8
46.1
13.6
40.7
101.7
Bottles,
36 in. belt width; TPH = 20 FPM/100 FPM x 0.7 TPH = 0.14 TPH
'Conveyor Speed = 100 FPM
2No idlers
3Densities as per Table 2-5
4Surcharge Angle = 5°
Surcharge Angle = 30°
6Based on capacities published in CEMA "Belt Conveyors for Bulk Materials"
                                    2-32

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        TABLE  2.10.   APPROXIMATE CONVEYOR BELT CAPACITIES
                           (FLAT BELT  WITH  6-IN.  HIGH
                          SKIRTBOARDS) 1'6 (TPH)
                                                    Belt Width (Inches)2
Component3
 18
24
36
48
60
72
Glass Bottles4

Plastic Bottles4

Aluminum Cans4

News5

OCC5

Loose Refuse5

Refuse from Compactor Truck5
34.0    47.4    75.1   104.1   134.4   165.9

 4.4     6.2     9.8    13.5    17.5    21.6

 4.4     6.2     9.8    13.5    17.5    21.6

13.6    19.9    34.7    52.1    72.3    95.1

 4.0     5.9    10.2    15.3    21.3    28.0

12.0    17.6    30.6    46.0    63.8    83.9

30.0    44.0    76.5   114.9   159.4   209.8
EXAMPLE: To find capacity at other belt speeds: New belt speed = 20 FPM; Plastic Bottles,
36 in. belt width; TPH = 20 FPM/100 FPM x 9.8 TPH = 2.0 TPH
1Conveyor Speed = 100 FPM
2No idlers
3Densities as per Table 2-5
4Surcharge Angle = 5°
5Surcharge Angle = 30°
6Based on capacities published in CEMA "Belt Conveyors for Bulk Materials"
                                      2-33

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     Most flat belt conveyors rely upon the friction force between
the head pulley  (drive pulley) and the conveyor belt to drive the
conveyor.  Where particularly heavy  loads are anticipated (e.g.,
MSW), chains are attached to the underside and to each side of the
belt  for  the   full  length.    This  configuration  usually  is
accompanied by cleats attached to the carrying surface of the belt
as  well  as  full length  skirtboards to  retain  material  on  the
conveyor.  ASME/ANSI B 20.1 Safety Standard is equally applicable
to flat belt conveyors as  it is to the  trough type as previously
discussed.

     Apron Conveyor

     An apron conveyor consists of steel pans (flat or contoured)
supported  by chains  and is  used in applications in which  the
conveyor may be  subject  to substantial impact and abuse.   Guide
rollers  riding   on  steel rails  minimize  the frictional  forces.
Cleats may be incorporated on the pans for inclined applications.
Apron conveyors  are often employed as infeed conveyors and may be
located in a pit  below floor level.  Ample  provision should be made
for  access for  cleanout and  maintenance.    Section  6.5  of  the
ASME/ANSI  B  20.1 Safety  Standard is specifically applicable to
apron conveyors.

     Screw Conveyor

     The screw conveyor  (or  auger) may  be used  to transport dry,
dense, free flowing materials  (e.g., tin cans formed as nuggets).
Screw  conveyors  have also been  used for bin  discharge  and as
metering feed devices.  These units are not designed to transport
stringy,  abrasive, or very wet materials.

     Pneumatic Conveyor

     A pneumatic conveyor  utilizes   a  stream of  air to  convey
suspendable materials (e.g.,  aluminum cans or dust)  through a tube.
Pneumatic  conveyors  may utilize  either a vacuum or  a  positive
pressure.  The pneumatic conveyor offers the facility designer more
flexibility in equipment  location. However, the number of changes
in direction in  the  lines  should be  kept  to  a minimum since they
result in pressure (efficiency) losses as well as probable points
of stoppages and wear.

     2.3.10.2.2   Material  handling  equipment  (separation)—The
following equipment is employed to separate one or more materials
from the waste stream or substream.  It should be recognized that
none of these devices can be expected to be 100% effective.

     Magnetic Separator

     Magnetic separation  is a relatively simple unit process and is
used to recover  ferrous metal from the commingled waste stream.

                               2-34

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Magnets may be either of the permanent or the electromagnetic type.
They  are available  in three  configurations,  namely,  the  drum
(Figure  2-13),  the magnetic head  pulley  (Figure 2-14),  and the
magnetic belt  (Figure 2-15).  They may be assembled and suspended
in  line,  crossbelt,  or mounted  as  conveyor  head pulleys.   The
magnetic head pulley conveyor is arranged so that in its operation,
the material  to be sorted is  passed over the pulley in  such a
manner that the nonferrous material will fall  along  a different
trajectory  than will  the  ferrous  material.    The  drum  magnet
assembly can  be installed  for  either overfeed  or underfeed and
directs the ferrous along a trajectory other than that taken by the
nonferrous material.   The magnetic  belt,  in  its  simplest form,
consists of single  magnets  mounted between two  pulleys that support
a cleated  conveyor belt mechanism.   The efficiency  of  magnetic
separation is affected by  the bed depth of the waste stream.   For
more complete  removal  of  ferrous,  a secondary magnetic separator
may be considered.  Conveyor and hopper  components in the vicinity
of  the  magnetic  field  should  be   constructed  of  nonmagnetic
materials.  Additional  information on magnetic separation can be
obtained in References 1 to 7.

     Eddy Current Device (Aluminum Separator)

     An aluminum separator employs either a permanent magnetic or
electromagnetic  field  to   generate  an electrical  current  (eddy)
which causes  aluminum  cans (nonferrous  metals)  to be  ejected and
separated from other materials.  Aluminum separation may take place
in the form of a conveyor head pulley or in the form of an inclined
stainless  steel  plate.    Additional  information  on  aluminum
separation can be found in References 7 to 10.

     Disc Screen

     A  disc  screen  consists  of  parallel multiple  shafts  all
rotating in the same direction.  Discs are mounted on each of these
shafts, and spaced  in such  a fashion so that the discs on one shaft
are located midway between the discs on an opposing  shaft.   The
shafts and  discs are  so positioned  relative  to  each  other as to
establish fixed  interstices through  which the undersize material
(e.g., broken glass or  grit) will pass and the  oversize material is
conveyed by both the discs and the series of  rotating shafts.  A
schematic view of a disc screen  is  presented in Figure 2-16.  Disc
screens are subject to damp and  stringy material wrapping around
the shafts  and discs  and  thus reducing the interstices.   At the
infeed location, abrasive material  (e.g., broken glass or grit) may
abrade the  outside diameters of  the shafts  and discs so as to
substantially  increase the interstices.   Also, large pieces of
corrugated  may  act  as a  barrier to smaller  material  dropping
through  the  interstices.    Any of these  conditions  can  have a
significant detrimental effect upon performance.
                               2-35

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            Magnet

Commingled Containers
  (2
    Deflector
                                              "'•  Gleaned
                                                F e rr o u s
                                              <=» Product
                              Small Nonferrous
                 (E
             Nonferrous Collection Conveyor
       Figure  2-13.  Multiple  magnetic drum.
                                             Nonferrous
                                             Product
                          Ferrous ^Splitter 
-------
                                 ,
                Nonferrous Material 1°
            Figure  2-15.   Magnetic belt.
                      .Large Material
                                 T      ,
                      Small Material
                       Side View
            y
Cylinders    Discs
                     /
                     Top View
                                                 Discs
             Figure  2-16.   Disc screen.



                           2-37

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      Trommel  Screen

      The   trommel   is   a   rotary   cylindrical   screen,  generally
downwardly inclined, whose screening surface consists of wire mesh
or  perforated plate.   A  diagram of a  typical  trommel screen  is
presented  in Figure  2-17.    The  tumbling action  of the  trommel
efficiently brings about a separation of individual items or pieces
of  material that may be  attached to each other,  or even of one
material contained  within another.  Large trommels  (8  to  10  ft  in
diameter,  and up to 50  ft long)  have been used to  separate  large
OCC  and/or newsprint from mixed paper  or  commingled  containers
(particularly from glass containers).  Small trommels  (1 to 2  ft  in
diameter,  by  2 to 4 ft long)  have been used to separate labels and
caps  from  crushed glass.  These small units are sometimes  used  in
conjunction with an air stream to aid in the separation.

      Two-stage trommels have also been  used in waste  processing.
In  two-stage trommels, the   first stage  (the  initial length  of
screen) is provided with small apertures  (e.g.,  1 in. diameter)
which permit broken glass, grit, and other small  contaminants  to  be
removed.  The second stage is provided with larger apertures (e.g.,
5 in. diameter) which allow glass, aluminum,  and  plastic containers
to be removed from  the  waste stream.   In the particular types  of
MRFs  discussed  in this document,  the oversize  materials  (overs)
might consist primarily of OCC and news,  depending upon the  make-up
of the incoming  waste stream.

      Many  factors influence the separation efficiency of a  trommel
including:

      •     characteristics and quantity of the incoming materials;
      •     size,   proportions,  and inclination  of   the  cylinder
           screen;
           rotational speed; and
      •     size and  number of  screen openings.

     Vibrating Screen

     A vibrating screen utilizes  a wire mesh or perforated plate
screen deck to separate  relatively dense, dry, undersize materials
from  less  dense oversize  materials.    A  schematic diagram  of  a
vibrating screen is given  in  Figure 2-18.  Vibrating conveyors are
more tolerant of stringy materials than are other conveyors.

     Damp,   sticky materials  have  a tendency to blind the screen
deck and thus impair the performance.   Large pieces of corrugated
and/or excessive material bed  depth  can substantially decrease
separation efficiency.
                               2-38

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              Side View
                                 Motor
                           Screen Surface
               End View
 Figure 2-17.   Trommel screen.
Figure  2-18.  Vibrating  screen.



               2-39

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     Oscillating Screen

     An oscillating screen is configured in a similar fashion as a
vibrating screen except that the motion  is of an orbital nature in
the plane of the screen deck.  The same comments as those presented
for vibrating screens apply.

     Traveling Chain Curtain

     The traveling chain  curtain  consists of one  or more rows of
common chain each suspended from a continuously revolving link-type
conveyor chain  describing a  somewhat elliptical  orbit  around a
vertical axis.  The curtain provides a barrier to less dense (e.g.,
aluminum and plastic) containers while permitting denser material
(e.g., glass) to pass through on a downwardly inclined surface.
The  efficiency  of  the traveling  chain curtain  can be  greatly
influenced by the feed rate into the unit. Excessive quantities of
incoming material may cause lighter materials to push through the
curtain  rather than to  be  directed  to one  side.    Detailed
discussions  about screens commonly used in the waste processing
field can be found in References 6, 7, and 11 to 16.

     Air Classifier

     Air classification employs an air stream to separate a light
fraction (e.g., paper  and plastic) from a heavy  fraction (e.g.,
metals and glass) in  a waste stream. Variables other than density,
such  as  particle  size, surface  area,  and drag, also affect the
process  of  material   separation  through   air  classification.
Consequently, aluminum  cans,  by virtue  of a high drag-to-weight
ratio, may appear in the light fraction, and wet and matted paper
may appear in the heavy fraction.

     Air classifiers may be provided in one of a number of designs.
The vertical, straight type  is  one of the most  common units. Air
classifiers  require  provisions  for appurtenant dust collection,
blower, separation,  and conveying.  Schematic diagrams of typical
air classifiers are provided in Figure 2-19.  A considerable amount
of work has been carried out in the area of air classification of
solid  wastes.   Results of  some  of  this work  are reported  in
References 7 and 17 to 22.

     2.3.10.2.3  Material handling equipment  (size reduction)—
Several  types of size reduction  equipment  are  used for  waste
processing.  The equipment is employed to reduce the particle size
and/or increase the bulk  density of material  in order  to  meet
market specifications  and/or to  reduce  the  cost of  storage and
transportation.
                               2-40

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Light
Fraction i





t
1
1
1
1
1
1
I


ft


tf




	 Shredded
j MSW Feed
\>
'N/
           Air
                   Heavy
                  Fraction
              Air
    Light Fraction
   Heavy Fraction
                                      Shredded
                                      MSW Feed
Figure 2-19.   Vertical air classifiers,

                    2-41

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     Can Shredder

     A  can  shredder  is  employed  to  reduce  aluminum cans  to
particles of small size (less than 1 in.)-  The process increases
the  density  and  thereby  conserves  on  transportation  costs.
Shredded aluminum  may command a premium price.   The shredder is
often supplied complete with infeed conveyor, magnetic separator,
blower, and  dust collector.  Due  to the costs  involved  in size
reduction,  prior  to the  installation  and  operation  of   a  can
shredder  it   is  especially  important  to   determine  if  the
specifications call  for shredded aluminum.

     Can Densifier/Biscuiter

     A can densifier is used  to  form aluminum cans into biscuits
generally weighing on the order of 40 Ib each.  The capacity of a
densifier may be increased by placing the densifier in series with
and following a can flattener.  A densifier offers a viable option
to baling aluminum cans.  As with the can shredder, it is important
to verify that the  market  will  accept and pay  for  the biscuit-
shaped product.  The typical range of floor area requirements for
aluminum can densifiers  commonly used in MRFs  is illustrated in
Figure 2-20.   Production rates  as  a function  of  horsepower for
aluminum can densifiers are presented in Table 2.11.

     Can Flattener

     A can flattener is a  device used  for flattening aluminum or
tin cans.  It  is often provided  complete with inlet  hopper, belt
conveyor, magnetic separator and pneumatic discharge.  The crushing
mechanism generally consists of a steel drum with hardened cleats
rotating against a pressure plate,  or  vulcanized rubber pressure
drum, or one or more sets of steel crushing rolls or drums.
Overload protection and provisions  for  separating any liquids that
may still be in the containers should be incorporated  in the system
design.

     Figure  2-21  illustrates  the  typical  range  of floor  area
requirements for can  flatteners (with infeed conveyors) as commonly
used  in  MRFs.    Clearance should  be  provided  for  maintenance
although most  flatteners  are relatively light  and portable,  and
thus they can readily be moved to another location for maintenance
if necessary.   Typical production rates as a function of horsepower
for aluminum and steel can  flatteners are presented in Table 2.12.

     Glass Crusher

     A glass crusher  is used to reduce whole glass bottles to small
particle sizes  in order  to meet  market specifications.    Glass
crushers are often supplied with a feed hopper and conveyor.
                               2-42

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                        3'-6"
             10'-0"to
                                                   2'-0" to
                                                    4'-0"
                              8'-0"to12'-6"

Figure  2-20.  Typical range of dimensions for can densifiers,
      TABLE  2.11.
TYPICAL PRODUCTION RATES  (lb/hr) AND
HORSEPOWER  FOR ALUMINUM CAN DENSIFIERS
Lb/hr
300 - 500
600 - 900
2500 unflattened
3600 flattened
Wt. of
Biscuit (Ib)
18
18

40
HP
K
7-1/2

25
                              2-43

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                                                3'-0" to
                                                  6'-0"
                        9'-0" to 18'-0"
Figure  2-21.   Typical  range of dimensions  for can flatteners.
 TABLE 2.12.  TYPICAL PRODUCTION RATES (lb/hr) AND HORSEPOWER
               FOR ALUMINUM CAN FLATTENERS
Lb/hr
Aluminum
1 ,200 unflattened
2,000 unflattened
4,000 flattened
Steel
2,000 unflattened
Horsepower
Blower Flattener
5 5
5 7.5
7.5
to 10

Conveyer
1/3
1/2
1/2
                               2-44

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 Glass crushers  are units that typically  require  relatively hiqh
 maintenance because of the abrasive nature of the glass.  Specifi-
 cations from the users should be checked before glass crushers are
 included in the  design of a MRF since some  buyers prefer to perform
 their own crushing.  Glass crushing is a dust producing operation
 and provision should be made to address this condition.

     >Figure  2-22   illustrates  the  typical  range  of floor  area
 requirements for glass crushers used in MRFs.  Clearance should be
 provided for  maintenance although  most  crushers  are  relatively
 light and portable and thus could be readily moved, if necessary,
 to another  location for maintenance.   Typical production  rates
 versus horsepower  for glass crushers commonly  used in MRFs  are
 presented in Table 2.13.

      Plastics Granulator

      A plastics  granulator is used to size reduce  PET and/or HDPE
 containers  to a  flake-like condition.  The  granulated plastic  is
 generally shipped  in  gaylords.    Due to  the  relatively  large
 reduction in  volume,  substantial  savings  in  shipping  can   be
 realized  when  plastic   granulation  is   employed.    Plastics
 granulation  is an operation that requires a relatively high degree
 of maintenance and  may be  prone to dust generation.   As with
 crushed  glass,  markets  should be  checked  to  verify  that the
 specifications call for granulated  material.  Some potential buyers
 may wish to  maintain close control over the type of  plastic they
 receive- and believe that they are better able to do so by requiring
 that the plastic be baled  rather than granulated.

     Plastics Perforator

     Technically,  a plastics  perforator  is  not classified  as a
 piece  of  size  reduction  equipment.   However,  its  use  is  so
 intimately associated with that of a  baler that it  is included in
 this discussion.   A plastics perforator is used to puncture plastic
 containers  in order  to  increase  bale  density  with  resultant
 shipping  economies.   The  perforations also eliminate the need to
 remove bottle  caps  and improve baler  efficiency  since bales are
 easier to form.  Ample storage must be provided for the perforated
 containers so that the baler may be efficiently utilized.

     Baler

    _ A  baler is  one  of  the  most common pieces   of processing
equipment employed in a MRF.   A diagram of  a baler is presented in
Figure 2-23.   Balers  are  used for  forming  bales  of newsprint
corrugated,  high-grade paper, mixed paper, plastics, aluminum cans'
and tin  cans.    These  units  are available with  a wide  range  of
levels of  sophistication.    Some  balers are equipped for  fully
automatic operation while others demand a  considerable amount  of
operator attention.   If the design calls for  the use of the same

                               2-45

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                                                  4'-0" to
                                                   5'-9"
                          9'-6"to15'-9"
Figure 2-22.   Typical  range of  dimensions for glass crushers
                 (with infeed conveyor).
 TABLE 2.13.   TYPICAL PRODUCTION RATES  (TPH) AND HORSEPOWER
                FOR GLASS  CRUSHERS

TPHa>
1 -3
3-4
5-6
15

Crusher
1
1 to 2
1 to 2
7-1/2
Horseoower
Conveyor
1/3
1/2
1/2
1/2
           a) Most glass crushers will accept 1 gal glass jars.
                       Figure  2-23.  Baler.

                                2-46

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      ^    bale more than one  material,  it is extremely important
 that the baler selected be specifically designed for that purpose
 The market  specifications  which must be met should be determined
 before  a  baler is selected.   Not all  automatic tie  devices are
 alike.   The  number  and  size  of  baling wires,  as well  as the
 available  wire  tension,   must  be  adequate  for the  particular
 materials to be baled.

     _Figures 2-24 and 2-25 depict the typical range of floor area
 requirements  for  single-ram  and  two-ram balers  respectively as
 commonly  used  in  MRFs.    Clearance  should  be  provided  for
 maintenance and accumulation of finished bales.  Table 2 14 lists
 typical production rates for OCC versus horsepower for horizontal
 balers commonly employed in MRFs.  Typical dimensions,  densities
 and weights of bales  for a  variety of materials are given in Table
 2.15.   _A considerable  amount  of  research  as  well as test and
 evaluation of size reduction equipment has been carried out during
 the past 20  years.  Some sources of information include References
 6,  7,  and 23 to 33.

      2.3.10.2.4  Equipment for environmental control—In order to
 protect the  health and safety  of the work force as well as to gain
 the goodwill  and to   meet  environmental  requirements  of  the
 community in which the  MRF is located,  it often  is necessary to
 provide  environmental   equipment  above  and  beyond  that  which
 normally is supplied with the material handling, separation,  and/or
 size reduction  equipment.    Title  29  of  the   Code  of  Federal
 Regulations,  Part 1910, presents the Occupational Safety and Health
 Administration (OSHA)  Standards which must be met to provide for
 the safety and health of the workers.   Local  and/or regional codes
 or  legislation often  address the environmental relationship  of  a
 facility within the community.   In the planning and design phase of
 the facility  it is wise  to review those operations likely to cause
 distress  to  either the worker  or to the community (or both)   and
 seek ways  in  how to best ameliorate or eliminate  the problems.

     Dust Collection System

     Shredding,  granulating,  crushing,  baling,  and  screening
 generally  are  dust producing  operations.    Depending  upon the
 severity  (which often is  a function  of the volume of material
 handled)  of  the problem, the  solution can vary  anywhere  from a
 simple dust mask for the worker, to individual dust collection at
 each  of the  dust  producers,  to  one or  more  centralized dust
 collection systems to serve the total  needs of the facility   Dust
 collection systems include fans,  ducting, cyclones, and baghouses.

     Noise Suppression Devices

     The majority  of  the equipment used in MRFs  generate  noise
and/or dust.  As is the  case with dust  problems,  the solution to
noise problems can  be simple (e.g., hearing protection worn by the
                              2-47

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  TABLE 2.15.
TYPICAL DENSITIES AND WEIGHTS (45"x30"x62" BALES)*
         FOR BALED MATERIALS
                                          Bale
Component
Corrugated
News
PET
Aluminum Cans
Steel Cans
Solid Waste
Density
(Ib/cu ft)
25
30
24
15
30
38
- 33
- 40
- 32
- 46
- 60
- 54
Weight
(Ib)
1200
1450
1160
730
1450
1840
- 1600
- 1940
- 1540
- 2230
- 2900
- 2610
 *  Bale sizes, volumes and weights may vary by baler manufacturer,
    model, mode of operation, moisture content, and other factors.


 worker)  or  may require  sound  muffling .equipment  and/or  sound
 proofing at specific work locations or throughout the building, or
 isolation of  specific pieces of  equipment.

     Odor Control Equipment

     Odor control is not  generally a problem at a MRF unless the
 MRF  is processing  mixed MSW.    Odors can  often be  reduced or
 eliminated by minimizing storage  time  of raw materials or product
 followed  by   frequent   floor   washdown.     Other  odor  control
 technologies  include:

          improved dispersion;
          odor masking;
          wet scrubbing;
          carbon adsorption;
          catalytic incineration; and
          thermal incineration;

    _In  severe odor  conditions,  multiple  technologies may  be
required.   Each technology  may  be  accompanied by,  problems (in
addition to  capital and operating  costs) of its own and indeed, the
technology may not be acceptable  to  the  control agency or to the
complainants.
                              2-49

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     Heating, Ventilating, and Air Conditioning (HVAC)

     The  geographical  location  (and  the  associated  climatic
condition) of the facility has a major influence on the HVAC system
required, as does the  very building design  itself.    Some  MRFs
incorporate  enclosed sorting station  rooms  in which HVAC systems
can be more  effective  than for open  stations.  Area  heaters and
ceiling  and  wall  insulation  may also  be  employed._   Adequate
ventilation  must  be provided  to  control  fumes   which _ may  be
generated  by  material   handling  vehicles,   incidental  incoming
hazardous materials, and incidental welding operations.
2.3.10.3  Fixed Equipment Capacity—
     The  process   of  MRF   design
should  include   that  the
manufacturer's  rated  capacity  and  maximum capacity,  generally
expressed in  tons  per hour  (TPH)  for  conveying,  separating,  and
processing equipment, be established and guaranteed.  For equipment
in  a system  in which there  is no  redundancy,  it  is wise  to
incorporate extra  capacity,  i.e.,  surge or  maximum capacity,  in
order to compensate  for the inevitable downtimes.  Alternatively,
the equipment may be called upon to operate on an overtime basis.
Example:

A paper baler has  the  following characteristics  for  a specific
grade of paper:

     Rated Capacity:    25 TPH
     Maximum Capacity:  27.5 TPH

The baler will have the following schedule for normal operation:

     Number of hours per day:  8
     Number of days per week:  5

Assuming that the  baler  is  out of service for repair for 8 hours
during  a 1-week  period,  it  is necessary to calculate the options
for making up the loss in production.   The expected production can
be obtained  by multiplying  the  rated capacity by the  number of
hours of normal  operation.

     Expected production =25 TPH x 40 hr = 1,000 tons

The "actual" production,  however,  is  calculated based on only 32
hours of operation.  Thus:

     Actual production =25  TPH x 32 hr = 800 tons

Consequently, there is a  deficiency of production of 200  tons  (1000
tons -  800 tons).
                               2-50

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 The following  options can  be followed  in order  to makeup  the
 deficiency:

      Option  1

      The baler  could  be operated  for 7.3 hours  of overtime  at
      maximum capacity  (27.5  TPH).

           200 tons =7.3  hrs x 27.5 TPH

      Option  2

      The baler could be operated for 8 hours at rated capacity  (25
      TPH) .

           200 tons = 8 hrs x 25 TPH

     Option  3

     The baler  could be  operated for 80 regular hours at maximum
     capacity.

           200 tons = (80  hrs x 27.5  TPH) -  (80 hrs x  25 TPH)
           200 tons = 2,200 tons - 2,000 tons

 2.3.10.4   Fixed  Equipment Material  Recovery Efficiencies—
     As  discussed in  Subsection  2.3.5 and listed  in Table 2.6,
 there  are various factors  which  affect  the  recovery  rate  of
 materials.    As  shown  in Table 2.16,  the interaction  of  these
 factors  result  in a  fairly  broad range  of material  recovery
 efficiencies.

     In each case, the  low end of the efficiency range  indicated in
 Table 2.16 may be reached when the feed rate is heavy  and the time
 of  exposure  of the material  to the separation device is minimal.
 Conversely,  the  higher recovery efficiencies may be  realized at
 light feed rates  (e.g., where a can or  bottle  is not buried in the
waste  stream)  and the time  of exposure  of  the material to  the
 separation device  is maximized.

 2.3.10.5  Availability of Fixed Equipment—
     Availability is defined  as the  estimated portion  of time that
a particular  piece  of  equipment is  available  to  perform the work
 for which  it  is  intended.  This is  a concept  often  overlooked in
the equipment selection process. The concept of availability takes
on special significance when  the equipment  in question is one of a
series of machines as is generally the case  in a processing system.
For example,   assume that  a single processing line consists of 5
pieces of equipment served by 6 conveyors.   Also assume that,  for
the purpose^ of illustrating the concept, the availability of each
of the machines is 0.95 (i.e., each machine is  expected to be down
                              2-51

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   TABLE  2.16,
MATERIAL RECOVERY EFFICIENCIES FOR SEPARATING
 EQUIPMENT
 Machine
                    Typical Range of Material
                    Recovery Efficiencies (%)
Magnetic Separator (ferrous)
Eddy Current (aluminum)
Disc Screen
Trommel Screen
Vibrating Screen
Traveling Chain Curtain
Air Classifier
60
60
50
80
60
60
60
- 90
- 90
- 90
- 90
- 90
- 90
- 90
Source:  CalRecovery, Inc.
for repair, maintenance, pluggage clearance, power outage, etc., 5%
of the time that  it  might  otherwise be running).   Lastly,  assume
that the availability of each of the conveyors  is  0.99.  Then, the
availability of  the  total system  (i.e.,  the process  line)  on a
worst-case  basis  (i.e.,  any  given   machine  or  conveyor  is
unavailable when all others are available), is:

     Conveyors (99%)  6 x Machines (95%) 5 = 72.8%

     In other words, a  system using these machines and conveyors
all  in  line  in  this manner for a 40-hour period  would,  on a
worst-case basis, operate only 0.728 x 40 hours = 29.12 hours.
The  example   is  provided  to underscore  the  importance  of  the
concept,  and  is  not meant  to  suggest actual  availabilities of
specific equipment.

     Equipment and system availability can be improved in various
ways.  Some of these are:

     •    the selection of proven equipment with a documented and
          validated history;

     •    the selection of heavy duty equipment;
                               2-52

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          proper   system  design  which  anticipates  jam     and
          pluggages,  particularly  at  entrance,  transfer,   and
          discharge points (e.g., conveyors, discharge chutes,  any
          bends in system, etc.) and provides  for their relief or
          elimination;
          trained   operating   personnel
          limitations of the equipment;
who   understand   the
          trained  maintenance personnel who  can readily address
          downtime problems;

          preventative maintenance program;

          supply of spare parts with particular  attention to long
          lead items; and

          awareness, in the design phase, of the  interrelationship
          of equipment so that the discharge  from one machine is
          compatible with the operations  of downstream equipment
          (if capacities don't match, some sort  of surge capacity
          needs to be included).

2.3.10.6  Fixed Equipment Redundancy—
     Problems  related  to   capacity  and   availability  can  be
substantially  reduced  by  providing  multiple  machines  and/or
processing lines.  This concept is known as redundancy.  Judicious
use  of _ redundancy  in  a  design  implies  that   if  a machine  or
processing line is out of service for any reason, another machine
or line can be brought into operation.  Provision for redundancy,
however,   is  often  accompanied by a  requirement for  increased
capital expenditure,  not only for  the duplicate equipment but also
for  the  additional  building  space  necessary  to  house  that
equipment.

     A form of redundancy can be achieved by other less expensive
means, including:

          Use of common  parts.   For example,  standardizing belt
          widths, motor sizes, and other mechanical and electrical
          components will  reduce  the  spare  parts inventory  yet
          allow ready repair of equipment.

          Multiple-use equipment.   A paper baler, for example,  may
          be equipped to handle plastics,  tin, and/or aluminum.

          Using diverters, for example,  in anticipation of downtime
          of a  glass crusher for flint glass, may make it feasible
          to temporarily  divert that  material  to another  glass
          crusher for processing.
                              2-53

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     •    Markets may be available which suggest that redundancy in
          some  equipment, .. should  be  of minor  importance.    For
          example, there may be a market for PET in ground or baled
          form.   However, even at  some price  reduction  for the
          final  product,  it may be  wise  to plan  on  selling the
          baled  product  at  the  lower price  rather  than  incur
          additional  capital  and  operating costs which may  be
          associated with the  granulating process.

     Redundancy is a very important concept  in the  design of MRFs.
Redundancy  is  particularly important at points or sections  of a
system that are critical to the continuous operation of the plant.
The implementation  of  redundancy  must be  carefully balanced with
practicality and financial viability.

2.3.10.7  Sizing of Fixed Equipment—
     The   considerations  of   recovery  efficiency,   capacity,
availability, and redundancy discussed in the preceding section in
addition to anticipated fluctuations in the daily quantities of
materials received, the  size of the tipping floor, the number of
shifts planned for operating, budgetary constraints, and the degree
of risk  one is willing  to accept,  all influence  the  design and
selection of  individual pieces of  fixed  equipment.   It  must be
emphasized  that  average  daily  tonnages   calculated  by  simply
dividing the annual tonnage  by the  number  of operating days (see
Subsection  2.3.2,   Mass  Balance)   can be  quite misleading  when
designing and selecting equipment.

     If one ignores  budgetary constraints,  a  capacity safety factor
or multiplier,  ranging from 1 to 2 on the maximum daily tonnages of
materials  anticipated,  should be  considered.    For  example,  a
multiplier of unity would be  reasonable for equipment sizing if the
facility were designed with  total  redundancy (with each piece of
equipment  capable  of  handling the  full  load),   high  equipment
availability (proven equipment  and systems),  single shift operation
(with the option of operating a second shift), and a relatively
consistent  flow of  materials.   A  multiplier  of two would  be
reasonable for equipment sizing if the facility were designed with
little or no redundancy,  low  availability due to  the positioning of
many pieces of equipment in series,  two shift scheduled operation,
and large  fluctuations  in inflow  of materials.    For equipment
employed in the average MRF,  a  multiplier of 1.25 to 1.5 generally
is used.  The  unique  concerns relating to  the  sizing  of sorting
conveyors will be discussed  in Subsection 2.3.12.2, Sorting Rates
and Efficiencies.

2.3.10.8  Maintenance of Fixed Equipment—
     Early  in the design phase of  a MRF,  consideration should be
given to providing sufficient access to the fixed equipment for the
maintenance  and  repair  work  required  to  keep  the  facility
operational.   Preparation of  preliminary maintenance  procedures
(preferably with the assistance of the equipment supplier) similar

                               2-54

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 to those examples  illustrated  in Appendix C for  belt conveyors,
 magnetic separator,  trommel  screen, can flattener, and baler serve
 not only  to  identify and  evaluate  the  amount  and quality  of
 maintenance required  but also  to alert  the  designer to  those
 equipment components to which access  must  be provided.

 2.3.11  Rolling Equipment

     The review and  selection process of rolling equipment for use
 in a MRF employs much of the same rationale  as  that  outlined for
 the review and  selection  process   for   fixed  equipment.    The
 following  observations  concern  some   special   considerations
 associated  with rolling equipment.

 2.3.11.1 Rolling Equipment  Commonly  Found in a  MRF—

          bins
          containers
          floor scrubber
          forklift
          front-end  loader
          manulift
          skid steer loader
          steam cleaner
          vacuum/sweeper/magnetic pick-up
          yard tractor

 2.3.11.2  Rolling Equipment  Capacity—
     Rolling   equipment   (most  of  which  is  material  handling
 equipment)  must, of course, be  adequate  to perform  the tasks
 required  to   feed   the  plant,   perform  intermediate  material
 transfers,  and  to   load  out the  products.    Equipment  must be
 selected of adequate power,  speed, and size to handle  the tonnages
 anticipated.    If the  equipment  is  too  small,  the productive
 capacity of the entire plant  can be adversely impacted.  It  is also
 possible for the  equipment to be  too  large for  the plant in that
 there may not  be  enough room to maneuver.

     The information presented in  Table 2.17 is provided as  a guide
 in  the  selection of an  appropriate  bucket size  for  a front-end
 loader handling the materials generally processed in a MRF.

 2.3.11.3  Availability of Rolling Equipment—
     Rolling equipment should be considered as an integral part of
the_ process line  of a MRF.   Downtime  associated with  rolling
equipment which delivers material  to an infeed conveyor, transfers
material to or  from various processes,  or loads the product into or
onto outgoing  trucks,  trailers,  etc., affects the  overall plant
availability just as does  fixed equipment downtime.  The same list
of considerations provided under that  for fixed equipment apply to
rolling equipment.
                              2-55

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       TABLE  2.17.   EXAMPLES  OF FRONT-END  LOADER CAPACITIES
Component
Whole Containers
Glass
Plastics
Aluminum
News
OCC
Loose Refuse
Refuse after
dumping from
compactor
truck
Average Loose Bulk Density3)
(Ib/cu yd)
500
65
65
170
50
150
375
Approximate TPH per cu yd Bucket
Capacity of Front-End Loader*3)
7.50
1.00
1.00
2.60
0.75
2.30
5.60
a)The values used are averages of a range of available data for each component.
b)For other front-end loader capacities, multiply the relative bucket size.
  Bucket size = 2-1/4 cu yd. Glass = 7.5 TPH/cu yd x 2.25 = 16.9 TPH.
                                        2-56

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 2.3.11.4    Rolling Equipment Redundancy—
      The  requirement  for redundancy in rolling equipment is not as
 severe as that for fixed  equipment.   Standard models  of  various
 pieces of  rolling  equipment  are  often  readily  available  for
 temporary or emergency use from a local dealership.  Often,  as part
 of a maintenance/service contract, a rolling equipment dealer will
 make ^ available a  replacement unit in the event that  a  particular
 machine  must  undergo extensive  repair.    Additionally,  various
 attachments to basic  machines may provide a degree of  redundancy
 through multi-purpose use.

 2.3.11.5    Rolling Equipment Selection—
      In the review and selection process  of individual items  of
 rolling  equipment, just  as  for fixed  equipment,  it  should  be
 recognized  that these items must not only compatibly interrelate
 with  one ^ another,  but also with  the  manner  in which  the  raw
 material  is to be received, the  in-process material  transferred,
 and the product loaded for shipment.  Special care should be given
 as to whether or not the vehicle is  to be used exclusively  indoors
 or  outdoors,  or  both,  particularly  in regard to  exhaust  fume
 generation.

 2.3.12  Human  Factors

     The  purpose   of  this  section  is  to  explore  a  few  of  the
 psychological  and physical  relationships  that arise  as  workers
 interact with machinery in  a MRF  environment.

 2.3.12.1  Staffing Requirements—
    _Whether  a MRF utilizes  a  low-  or high-technology   system
 configuration or some intermediate system,  there is a  need  for the
 employment  of  manual  laborers.    In  another section of this
 document, job^descriptions, employee relations,  health and  safety,
 and other topics will be discussed.  The information presented  in
 Table 2.18  is  provided  as  a guide to  the  size and make-up of the
 work force  in MRFs of various throughputs.

 2.3.12.2  Sorting Rates and Efficiencies—
     The  ranges  of  manual  sorting rates  and efficiencies for
 various materials are  presented in  Table  2.19.   In  a  mix of
 materials,  such as OCC and newspaper,  higher sorting efficiencies
 will^  generally be achieved  by  manually  removing  ("positively
 sorting")  the lesser quantities of material from the greater.  As
 shown in Figure 2-5,  in sorting  station  #1,  residue  at a rate of
 4.4 TPD and OCC at  a  rate  of about  9.8  TPD are positively sorted
 from the incoming mix of 44  TPD.  On  the other hand,  about 29.77
 TPD of newspaper are permitted to  pass through the sorting station
untouched (i.e., "negatively sorted").  With reference to sorting
 station #2,  in Figure 2-6,  mixed broken glass would be negatively
 sorted even though it represents a lower throughput than either
green or clear  glass since the broken glass would be more difficult
                              2-57

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     TABLE 2.18.   APPROXIMATE RANGE OF STAFFING REQUIREMENTS
                    FOR MATERIAL RECOVERY  FACILITIES
Tons per Week
Personnel
Office
Plant Manager
Scalemaster/ Bookkeeper
Clerk
Janitor
500

1
1
0-1
0
1,000

1
1
1-2
0
1,500

1
1
2-3
0
2,000

1
1
2 -
1

3

 Plant
    Foreman/Machine  Operator   1-2     2-3
    Sorters                    13  -  25  16 - 27
    Forklift/FEL Operators     2-3     3-4
    Maintenance                    1         2
                     3-4     3-4
                    19 - 32   25 - 38
                     4-5     5-6
                       3         4
          TOTAL
19 - 34   26 - 40   33 - 49   42  - 58
Source:   CalRecovery,  Inc.
        TABLE  2.19.  MANUAL SORTING RATES AND  EFFICIENCIES

Material Containers/lb

Newspaper •• •
Corrugated — --
Glass
(mixed/whole) 1 .5 - 3.0
Glass
(by color) 1 .5 - 3.0
Plastic
(PET. HOPE) 4.5 - 9.0
Aluminum
(from plastic) 22.5 - 27
ADoroximate Ranges
Containers/Minute/ Lb/Hr/Sortera'
Sorter
1 500 - 1 0 000
1 500 . •) o 000
30 - 60 900 - 1 ,800
1 5 - 30 450 - 900
30 - 60 300 - 600
30-60 100- 120 '

Recovery
Efficiency (%)
60-95
60-95
70-95
80-95
80-95
80-95
        a) Based on average sorting rates (containers/minute/sorter).

                                 2-58

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 to  manually  extract  from  the  glass  stream  than  whole glass
 containers.

      Sorting  stations  should be  arranged so that the sorters are
 not competing with  one another for the same  item.   Some designers
 accomplish this by positioning the sorters on only one side of the
 sorting belt  and by assigning specific materials  to be handled by
 each  sorter.  Other designers locate the  sorters  on both sides of
 the  sorting  belt.   In  this particular situation,  the   sorting
 positions are staggered  along the belt  length  in order to avoid
 competition by more than  one  sorter over the same item. Appropriate
 widths for  sorting  belts,  selected to minimize personnel  fatigue
 and consequent loss of efficiency,  are given in Table 2.20.  The
 working height of the sorting belt should be between 36 in.  and 42
 in. from the platform level.  A working height of 42 in. allows for
 the installation of temporary risers for  shorter  workers.

      Sorting belts should be outfitted with variable speed  devices
 capable of controlling the belt speed between 0 and 100 FPM.  The
 higher belt speeds would  be utilized under conditions where  most or
 all of the material is anticipated to be negatively sorted.  For
 average sorting conditions  for both  paper sorting  and commingled
 container sorting,  a maximum belt speed  of  30  FPM is considered
 appropriate.     Sorting   rates  and   manual  material   recovery
 efficiencies may be further enhanced  by providing  the  sorting area
 with  complete environmental  control  (i.e.,  heating, ventilation,
 and air conditioning).   This approach will  also reduce personnel
 exposure to process noise and dust.

 Sample Calculations (Paper)

 Refer to Figure 2-5, Paper Line - sorting station #1
 Incoming paper =44 TPD  (5.5 TPH)
 Design capacity = 1.5 x 5.5 TPH =8.25 TPH
 To find combined density:
     Newspaper (6.19 Ib/cu ft) x 29.77 TPD = 184.3
     OCC (1.87 Ib/cu ft)  X 9.83  TPD =18.4
     Residue  (150 Ib per cu yd/27)  x 4.5 TPD/44 TPD = 24.5/227.2
     Average density = 227.2/44  =5.16 Ib/cu ft

Capacities for flat belts (in cu ft/hr) at a speed of 100  FPM are
presented in Table 2.21.
                              2-59

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 TABLE  2.20.   RECOMMENDED  MAXIMUM SORTING  BELT WIDTHS
     Sorting Process
                                    Recommended Maximum Belt Width (in.)
    Sorting Stations
     on One Side
                 Sorting Stations
                  on Both Sides
   Paper (OCC or ONP)
   Commingled Containers
         42
         30
                      72
                      48
                TABLE 2.21.   FLAT BELT CAPACITY20
                                   Capacity at 100 FPM (cu ft/hr)
                                        Surcharge Angle
    Belt Width
      (in.)          5°
10°
15°
                     20°
                     25°
                                           30°
18
24
30
36
42
48
54
60
72
84
96
120
234
378
552
768
1014
1296
1614
2352
3228
4243
246
465
756
1112
1542
2037
2604
3240
4722
6480
8514
372
702
1137
1677
2322
3072
3924
4884
7116
9768
12834
498
942
1527
2253
3120
4128
5274
6560
9558
13116
17238
630
1188
1926
2844
3936
5208
6654
8280
12060
16548
21750
762
1446
2340
3450
4776
6318
8076
10050
14640
20091
26406
a) Standard Edge Distance = 0.55b + 0.9 in. Adapted from CEMA "Belt Conveyors for Bulk
Materials."
                                     2-60

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      TABLE  2.21.    FROM  TABLE  2.21  AND SURCHARGE ANGLE  =  30'

42
Cu ft/hr at 1 00 FPM 4776
Cu ft/hr at 30 FPM 1433
Lb/hr at 30 FPM and 7394
5.16lb/cuft
TPH at 30 FPM and 3.7
5.16lb/cuft
Belt Width (in.)
48 54 60 72
6318 8076 10050 14640
1895 2423 3015 4392
9778 12503 15557 22663
4.9 6.3 7.8 11.3
                 Safety factors based on 5.5 TPH nominal feed rate:

                     54 in. belt with 6.3 TPH/5.5 TPH = 1.1

                     60 in. belt width 7.8 TPH/5.5 TPH = 1.4

                     72 in. belt width 11.3 TPH/S.5 TPH = 2.1

       TABLE 2.21.   FROM TABLE 2.21 AND  SURCHARGE  ANGLE
                                               =  5'
                            24
                  Belt Width (in.)

             30         36
   15.76lb/cuft

   TPH at 30 FPM and
   15.76lb/cuft
0.6
0.9
1.3
                           42
                           48
Cu ft/hr at 100 FPM
Cu ft/hr at 30 FPM
Lb/hr at 30 FPM and
234
70
1103
378
113
1781
552
166
2616
768
230
3625
1014
304
4791
1.8
2.4
Safety factor based on 1.77 TPH feedrate:

       36 in. belt width 1.3 TFH/1.77 TPH = 0.7

       42 in. belt width 1.8 TPH/1.77 TPH = 1.0

       48 in. belt width 2.4 TPH/1.77 TPH = 1.36
                                        2-61

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Conclusion

     In the example chosen, a width of 72  in.  for the sorting belt
at a speed of  30  FPM is an option which would provide sufficient
capacity to accommodate material surges of 50% of the nominal feed
rate.  Consequently,  lacking budgetary constraints,  this belt is
the recommended choice  for this particular application.

Sample Calculation  (Commingled Containers)

Refer to Figure 2-6, Commingled Container  Line—sorting station #2

Incoming containers = 14.18 TPD (1.77 TPH)
Design capacity = 1.5 x 1.77 = 2.66 TPH

To find combined density:
     Glass (18.45 Ib/cu ft) X 11.35 TPD = 209.4
     Ferrous (4.9 Ib/cu ft) x 0.62 TPD =3.0
     Aluminum  (2.36 Ib/cu ft ) x 0.10 TPD =0.2
     Plastic (2.37 Ib/cu ft) X 0.23 TPD =0.5
     Residue   (150  Ib  per  cu  yd/27)  x  1.88 TPD/14.18  TPD  =
     10.4/223.5
     Average density =  223.5/14.18 = 15.76 Ib/cu ft

Conclusion

     In the example chosen, a width of 48  in.  for the sorting belt
operating at 30  FPM is the  only possibility  which would provide
sufficient capacity to  accommodate any material  surges (and that
would be approximately 36% over the nominal  feed rate).  It is not
suggested that a wider belt be used since  that would reduce worker
efficiency.   If necessary,  for short periods of  time,  the belt
could be operated at a higher speed (2.66 TPH/2.4  TPH x 30 FPM =33
FPM) in order to reach  a 50% surge capacity.

2.3.12.3  Psychological Factors—
     In  the  long  list  of  services  and  processes provided  by
individuals and organizations in the communities which make up our
society, few may be regarded as more  beneficial  to and necessary
for our society than those associated with a MRF.

     Much can be done to enhance the status of the manual laborer
both in the eyes of the public as well as in his or her own eyes.
They include, among others:

     •    conducting  an active and continuing public  relations
          campaign siting the important contribution a  MRF makes in
          improving the quality of life;

     •    designing  and building  a MRF  which is aesthetically
          pleasing both to the visitor and to the worker;
                               2-62

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           developing a sense  of pride and accomplishment  in the
           mind of each worker for a difficult task well done; and

           maintaining the MRF in  such a  manner as to  make  it as
           pleasant a place as possible in which to work.

 2.3.12.4  Physical Factors—
      As is true with many processing and/or manufacturing plants,
 workers  in  a  MRF  must  interact  with  both  fixed  and  rolling
 equipment on a  continual basis.  In a MRF, the incoming materials,
 particularly bottles (broken glass) and cans (sharp, ragged edges),
 present physical  dangers to  the worker as   does the  equipment
 employed in handling and  processing that  material.

      In addition to the attention which must  be paid  to providing
 each worker  with  safety  clothing  and  equipment  and  otherwise
 adhering to the general industrial safety practices (OSHA),  there
 are  a  few  special  precautions  to  observe   in the  design  and
 operation of a  MRF.   They  include,  among  others:

           incorporating a  system in  which the worker  monitors the
           machine.   This is to ensure that the machine operates as
           intended and  is  not  overloaded;

           incorporating a system in which the  machine  monitors the
           worker.   This is to ensure that should the worker,  for
           whatever reason,  not perform the task as intended,  the
           machine  will  issue a warning or shut  down;

           adopting an operating philosophy that the worker is  not
           in  competition  with the machine,  but rather that  the
           worker  and machine complement  one  another  in order to
           best  perform  the task;

           designing  the work stations in such  a manner as to limit
           the physical  exertion  and awkward bending,  stretching,
           lifting, and  moving required to perform the task;

           arranging  equipment controls in a simple and consistent
          manner from machine  to  machine  to reduce the chance of
           operator error;  and

          recognizing the probability of fatigue or boredom because
          of the routine nature of the  tasks and adjusting working
          schedules and/or task assignments accordingly.

2.3.12.5  Employment Opportunities—

     In communities of high or chronic unemployment (particularly
of unskilled laborers), MRFs present an opportunity to alleviate
that condition.   The MRFs  also  provide  an  opportunity  for  the
                              2-63

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employment  of  part-time seasonal  workers typically  required  in
resort areas.

2.3.13  Acceptable Waste

     Acceptable waste may be defined as that material which the MRF
is designed to  receive and process for the markets identified.  For
the basic MRF as described in Subsection 2.2.1, acceptable waste is
identified as source separated materials arriving at the facility
in  two waste  streams,   i.e.,  paper  and  commingled  containers.
Variations from the basic MRF which broaden the list of acceptable
waste are discussed in Subsection 2.2.2.

     The  quality  of the   incoming   waste materials  is  highly
dependent upon  the understanding, cooperation,  and participation of
the public.  In order to increase the probability of the facility
receiving acceptable waste,  it is wise to publish a list, not only
of acceptable waste and how to prepare it, but also of waste that
is unacceptable.  One such list is shown on Table 2.22.

2.3.14  Raw Material Storage

     The design of most MRFs incorporate sufficient  storage area to
accommodate  the  equivalent  of at  least one day's supply  of raw
material.  Several  factors influence  the  decision regarding the
amount of floor space to allocate to raw material.   They include:

          Redundancy. A facility with redundant processing systems
          has less need for raw material storage space.

          Processing  vs receiving hours.   A  facility open  to
          receipt of raw material outside  of scheduled processing
          times must  provide  sufficient storage  capacity for the
          raw material.   In the case where scheduled processing
          takes  place  (e.g.,  a  second  shift)  beyond  the  MRF
          receiving hours, raw material storage is also necessary
          in order to provide the material to process.

          Local regulations.  In many localities restrictions are
          placed upon the number of vehicles which may queue up to
          unload.   Adequate raw  material storage space must  be
          provided to prevent this condition from occurring.

     «    Vehicles  vs  tipping  floor  configuration.    The  mere
          provision of floor space  for the storage of raw materials
          may  not  totally  address the  problems  discussed  above.
          Care must be taken that the  collection vehicles can gain
          ready access  to the  tipping floor,  quickly unload, and
          depart with a  minimum of interference with other vehicles
          and/or the  front-end loader(s) on the tipping floor.
                               2-64

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TABLE  2.22.
MATERIALS TO  BE  COLLECTED  FOR  RECYCLING  NEWSPAPER,
WHITE  OFFICE  PAPER,   CORRUGATED CARDBOARD,  GLASS,
TIN  CANS,  ALUMINUM,   AND PLASTICa)
Acceptable
(Common Names)
                  Non-Acceptable
   Preparation
 Paper
   Newsprint
   White office paper
 Cardboard
   Corrugated
              Glossy paper
              Magazines
              Phone books
              Colored office paper
              Any waxed cardboard (i.e., milk
              cartons)
              Any corrugated contaminated
              with food or other waste
Remove any tape,
rubber bands, or
staples
Flatten corrugated
 Glass
   Bottles (any color)
   Jars (any color)
Aluminum
   Aluminum beverage cans,
   foil, aluminum pie plates

Tin Cans
   All tin cans
 Plastic
   Only consumer (i.e., high
   density polyethylene [HOPE],
   shampoo bottles, detergent
   bottles, milk and water
   bottles, oil, anti-freeze
   containers)
   PET = beverage containers
              Plate glass (window)
              Light bulbs
              Drinking glasses
              Ceramics of any kind
              Construction aluminum
              Unwashed cans
              Any brittle plastics (i.e.,
              cottage cheese containers)
              Film (i.e., plastic bags)
              Ketchup bottles
              Industrial plastic
Do not break
Rinse
Remove tops, rings
and caps
May leave paper labels
Rinse and clean
Rinse can
Remove label
Do not need to remove
both ends or flatten
Remove caps and rings
Rinse container
Flatten if possible
a) For example purposes only.
                                         2-65

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2.3.15  Product Storage

     The amount and location (i.e., indoors or outdoors)  of space
allocated to product storage is influenced, in great degree, by the
markets.   Paper  products may be stored  indoors  in  bales,  loaded
loose into compactor type transport vehicles, or baled and loaded
into trailers or rail cars. Often  the  market will  dictate on how
the product is to be shipped.  Aluminum cans, tin cans and bimetal
cans may be shipped loose,  flattened or otherwise size reduced and
shipped.  The market specifications will  also influence whether or
not the  products may be  stored  outdoors pending shipment.   The
finished forms of  other products as well have  been  discussed in
Subsection 2.2.1. and  included in Tables 2.2 and 2.3.  In any case,
sufficient space must be allocated  indoors or outdoors in order to
make an economic shipment of the product to the market.

2.3.16  Building

     The MRF building design should be  a  joint effort on the parts
of the process engineer,  structural  engineer,  and the architect.
The design will necessarily be influenced by the site conditions
and anticipated  traffic patterns.   Clear, wide  bays  utilizing a
minimum  number of  interior columns  are preferred  in order to
present  the least  possible interference with  trucks and other
rolling equipment.  A high bay tipping floor is often a requirement
for the accommodation  and dumping of raw material.  Similarly, wide
high  bay  doors  are   desired  to  minimize  the  possibility  of
interference with tipping vehicles.

     Consideration should be made in the design of the building for
the possible  future expansion  of the  facility  to  handle greater
quantities  and/or an  increased  variety  of  raw materials.   The
building should also be viewed  as a tool  for the mitigation of any
noise, dust, litter, and odor that might otherwise adversely impact
upon  the surrounding neighborhood.    Enclosed,  well  illuminated
sorting  rooms with  properly designed  HVAC systems  will  assist in
maintaining a high level of productivity and worker morale.
Obviously, all building, fire, and safety codes must be adhered to.

2.4  MRF MANAGEMENT

2.4.1  Organization

     A nationwide  survey of MRFs  (Table  2.23)  gives  a  numerical
breakdown of employees by management and  nonmanagement categories,
and by  size of  facilities.   The  total  number of  employees per
existing facility averages about 19.  Planned  installations at the
time of  the survey, showed a higher workforce,  approximately 26;
however, these  planned facilities  are larger  in design capacity
than current plants.
                               2-66

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          TABLE 2.23.
      NUMBER OF FULL-TIME  EQUIVALENT
      (FTE)  EMPLOYEES
Sample
                 Standard
Mean    Sum   Deviation  Minimum  Maximum
TOTAL EMPLOYEES
All Facilities
Planned Facilities
Existing Facilities
MANAGEMENT
All Facilities
Planned Facilities
Existing Facilities
NON-MANAGEMENT
All Facilities
Planned Facilities
Existing Facilities
21.67
25.69
18.55

2.87
3.56
2.34

18.79
22.13
16.21
RATIO OF NON-MANAGEMENT
All Facilities
1 to 99 TPD
100+ TPD
Planned
Existing
Low-Tech
High-Tech
0.272
0.385
0.142
0.159
0.360
0.313
0.210
1,538
796
742

204
110
94

1,334
686
648
23.37
28.56
18.17

2.96
3.57
2.28

20.94
25.69
16.22
EMPLOYEES: DESIGN
-
-
-
-
0.442
0.578
0.142
0.155
0.561
0.582
0.130
1.50
8.00
1.50

0.10
1.00
0.10

1.00
7.00
1.00
CAPACITY
0.035
0.044
0.035
0.035
0.044
0.058
0.035
165.00
165.00
92.00

16.00
16.00
12.00

150.00
150.00
80.00
(TONS PER
3.500
3.500
0.468
0.900
3.500
3.500
0.535
71*
31
40

71
31
40

71
31
40
DAY)
71
38
33
31
40
38*
31
  No information was available from 33 planned MRFs with regard to number of
  employees (management or non-management); an additional two projects did not
  furnish data with respect to degree of mechanization.
                                 2-67

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     Data relating the ratio  of  nonmanagment  employees to design
capacity are  given in  Table 2.24.   This  ratio  can  provide  an
indication  of operational  effectiveness,  as  labor  costs are  a
significant  part  of  total  operation  and  maintenance  costs.
However, lower labor requirements normally result from the use of
fairly sophisticated equipment.   The increased capital costs must
then be equated with lower costs  before a judgement on operational
efficiency can be made.   In Table 2.23, the ratios of employees to
different categories of MRFs is also given.   These types include:
plants processing 1 to 99  TPD, and greater  than 100  TPD; planned
and existing facilities; and "low" and "high-tech" plants.

2.4.2  Operating Schedules

     The majority of MRFs surveyed  (GAA, 1990) processed materials
on a  5-day  per week basis.   The mean figure,  as  shown in Table
2.24, actually  is  5.23  days per  week with a  range of 4.0 to 6.5
days per week.

     Most of  the MRFs surveyed operated one  shift per day;  some
scheduled two or three shifts.   The mean value  for all facilities
was  1.16 shifts per day.   The length of a shift was 8 hours at
nearly all planned and existing facilities; however, a  small number
of existing plants had shifts ranging  from 4 to 10  hours.   The
average  number of days  that the  MRFs  were  in operation _ varied
between 208 and  338; the average number of days was approximately
266.

     It is  important  to  note that  the schedule of operations for
any  facility  will depend  on locally defined  conditions.   These
conditions  would include collection schedules,  throughput of the
facility, capacity of the  facility, etc.

2.4.3  Job  Descriptions

     A variety of skills  are required  for  personnel  operating a
MRF.  Descriptions of jobs to be carried out at a MRF are discussed
in the following paragraphs.

2.4.3.1  Plant Manager—
     The plant manager works under the general supervision of an
operations  vice president.    The  plant  manager   directs  and
coordinates,   through   subordinate  supervisory  personnel,   all
activities  concerned with production of end  products  from the
recyclables.  The manager will confer with management  staff at the
corporate level to ensure achievement of established production and
$/annual  capacityquality  control  standards,  development  of and
compliance  with  cost controls, development of operational  budget,
and maintenance  of the safety plan.
                               2-68

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              TABLE  2.24.    OPERATING  SCHEDULES OF MRFs
 Sample
         Standard
Mean    Deviation   Minimum   Maximum    N
DAYS OF OPERATION PER WEEK
All Facilities
Planned Facilities
Existing Facilities
5.23
5.24
5.21
0.42
0.40
0.45
4.00
5.00
4.00
6.50
6.50
6.00
99
59
40
*  No information was available from five planned MRFs with regard to days of plant
   operation per week.                                                       r

SHIFTS PER DAY
All Facilities
Planned Facilities
Existing Facilities

   No information was available from six planned MRFs with regard to the number of
   shifts per day.
1.16
1.13
1.19
0.41
0.42
0.39
1.00
1.00
1.00
3.00
3.00
2.00
98*
58
40
HOURS PER SHIFT
All Facilities
Planned Facilities
Existing Facilities
 8.00
 8.00
 8.00
0.50
0.00
0.50
4.00        10.00      98*
8.00         8.00      58
4.00        10.00      40
   No information was available from six planned MRFs with regard to hours per shift.

DAYS OF OPERATION PER YEAR
All Facilities                    266.51
Planned Facilities               265.88
Existing Facilities               267.43

   No information was available from six planned MRFs with regard to the number of
   days of plant operation per year.
21.29
21.69
20.94
208.00
250.00
208.00
338.00
338.00
312.00
98*
58
40
                                     2-69

-------
2.4.3.2  Foreman—
     The foreman works under the  direct  supervision of the plant
manager.  The foreman is  responsible  for the daily production of
end products in specified  quantity  and quality  on both the mixed
recyclables and paper processing lines.   The foreman will conduct
start-up and close-down procedures before and after his shift and
ensure  that proper  maintenance  procedures  are followed  by  the
employees under his supervision.   Other responsibilities include:
inspecting load-out of materials; ensuring that all work stations
are maintained in a  clean  and  orderly manner;  and verifying that
all employees are  furnished with appropriate safety apparel  and
equipment.

2.4.3.3  Maintenance Mechanic—
     The maintenance mechanic repairs  and maintains,  in accordance
with diagrams, sketches, operations manuals, training programs, and
manufacturer's  specifications,   all  machinery  and  electrical
equipment relating to processing.  The maintenance mechanic  is also
responsible  for  performing maintenance  checks  before  and after
operations,  as well  as initiating  purchase  orders for necessary
parts  and supervising  general factory  workers in  cleaning  and
preventive maintenance tasks on  individually assigned equipment.
The senior maintenance mechanic reports directly to the foreman.

2.4.3.4  Equipment Operators—
     The  equipment  operator  is  responsible   for  movement  and
transfer   of  recyclables.    Each  operator  has   a  complete
understanding of  the MRF  systems,  and  is trained  to  assist in
material  inspection  and  quality  control.   The  operators on both
lines  are  responsible  for properly loading  material to assure a
fully  charged receiving pit and a well-mixed load, and to densely
and evenly load bales of processed material onto  transfer trailers.
One equipment operator  is responsible for facilitating baler-to-
trailer  loadout  of processed steel,  aluminum,  and plastic.   All
rolling stock operators and plant personnel are cross-trained for
versatility  and plant efficiency.

2.4.3.5  General Factory Workers—
     General  factory workers  are responsible  for color sorting
glass  and  separating HOPE and  PET plastics.  All  general factory
workers are  trained  to ensure that  contaminant-sensitive material
(e.g.,  glass)  is  free  of  deleterious   foreign  matter such as
ceramics, plate glass,  and porcelain.  General factory workers are
trained to recognize nonrecyclable material and  inform the foreman
if any potentially damaging or hazardous items are found  in the
process flow.  These are the only active  sorters on the processing
line.

2.4.3.6  Quality Assurance Inspectors—
     Quality assurance inspectors staff the mixed  recyclables  line
at  the  inspection  station.   The  inspector is  responsible  for
examining  the material  infeed  for contaminants and  nonrecyclable

                               2-70

-------
 materials.   A  dedicated inspector—not sorters preoccupied  with
 maintaining end-product  purity—is necessary to ensure the removal
 of these reject materials.

 2.4.3.7   Administrative  Assistant—
      The  administrative   assistant  works   under  the   direct
 supervision of the plant manager.   Duties of the  administrative
 manager  include:  "front office" tasks such as answering telephones
 and reception;  preparing and submitting all  required reports  such
 as material shipments, and  personnel record  keeping.

 2.4.4 Health  and  Safety Considerations

      It  behooves any employee of a  MRF to be alert  to  potential
 health   and  safety  problems  associated  with  the   workplace
 environment and the waste  stream processed.   There  are  physical
 dangers  inherent in the commingled  recyclables or MSW, such  as
 broken   glass,  sharp  metals, etc.    There  are  also  potential
 environmental and medical dangers, particularly in raw MSW, blowing
 dust, etc.

      Workplace dangers are also present  at a MRF.  Mobile equipment
 such^ as  fork  lifts,  front-end  loaders, and  delivery trucks are
 heavily  utilized; common sense safety procedures  must be followed.
 Further, the nature of a MRF processing  line  requires that certain
 functions be carried out at elevated heights.  With  this  in mind,
 there are steps to climb, sorting stations to tend,  etc.  Care must
 be exercised in getting  to  and  from  the work station, as well  as
 while working.   Safety helmets are a must, as a high probability
 exists that objects will  fall from an elevated station from time  to
 time.

      Good   safety   practices are  needed   at  any  MRF.    This
 necessitates a well-managed safety training program to inform the
 employee  as to what  constitutes "working  safely;"  this is  a
 fundamental management responsibility.

 2.5.  MRF ECONOMIC ANALYSIS

 2.5.1  Introduction

     The purpose of this section is to present a range of capital
 and  operating  costs  for  MRFs.  The  costs  for  the  facilities  are
 presented in two forms: unit costs, such as  dollars  per ton per day
 ($/TPD),  and in total cost for throughput capacities between 10 TPD
 and  500  TPD.   A range of throughput capacities  has been used to
 reflect  any resultant  economies  of  scale.   A range  of costs is
presented in order to account for variations in  both engineering
design and in capital and operating costs,  and to accommodate the
wide variety of specific conditions that apply to MRF projects.
                               2-71

-------
2.5.2  Composition of Recvclables

     In order  to perform the  cost  analysis for the  facility,  a
composition of recyclable materials  has been assumed.  The assumed
composition  of  recyclables  expected to  enter  the  facility  is
presented in Table  2.25.   Furthermore,  it  has  also been assumed
that commingled paper will arrive into the facility separated from
commingled containers (aluminum, steel,  plastic and glass).   This
coincides with the material flow assumptions presented in Figures
2-5 and 2-6.

2.5.3  Capital Costs

2.5.3.1  Facility Construction Costs—
     Estimated capital costs have been developed for both facility
construction and for equipment.  Ranges for  unit capital costs for
five major  construction  categories  are presented  in  Table  2.26.
The  difference   between   low  and  high   cost   ranges  include
project-specific conditions  such  as subsurface  conditions,  local
topography,  structural materials used for  building construction
(e.g.,  steel or concrete)  and local building code requirements.
Typical floor area requirements for the major sections  of a MRF are
presented in Table 2.27 as a function of throughput capacity.  As
indicated in the table, primary variables are the amount of tipping
floor and storage capacity  desired  for processed  recyclables.   A
general rule is  to maintain sufficient tipping  floor  capacity to
accommodate a reasonable "worst-case" unscheduled maintenance event
and enough storage capacity for one to two unit truckloads (about
20 tons/truck) for each material processed.

     The unit cost elements  given in Tables 2.26  and 2.27 have been
combined in  Table 2.28 to present total and unit construction costs
as a function of capacity.  As shown in the table, in the case of
facilities having a  capacity in the range of 10 TPD to  500 TPD, the
unit costs decrease as capacity increases.

2.5.3.2  Equipment Costs—
     Table 2.29  presents  a  range  of typical unit  equipment  costs
based  upon  the  throughput  capacity of  the  MRF.   Similar  to
construction  costs   of  the facility,   the  unit   costs  for  the
equipment decrease as capacity  increases.  Reasons  for  the decrease
in unit  costs include price reductions  generally  received  from
vendors for large purchases and economies  of scale obtained when
producing larger pieces  of equipment, at  least in the  range of
facility capacities considered herein.   Table 2.30 presents  total
equipment costs by throughput capacity.  The data in the table also
show a summary of equipment unit costs.

2.5.3.3  Total Capital Costs—
     Estimated  total capital  costs by  throughput capacity  are
presented in Table 2.31.   The information in the table is divided
into facility construction costs, equipment costs,  and  engineering

                               2-72

-------
 TABLE  2.25.    ASSUMED  RECYCLABLES  COMPOSTIONa)
               Material
                                   Percent by
                                     Weight
        Newspaper

        Mixed Paper

           TOTAL PAPER

        Glass Bottles

        Tin Cans

        Aluminum Cans

        PET & HOPE Containers

           TOTAL COMMINGLED CONTAINERS

             TOTAL
                                       33

                                       41

                                       74

                                       19

                                       4

                                       1

                                       2

                                       26

                                      100
       a) Recyclables are assumed to arrive at the MRF as commingled paper and
         commingled containers.
TABLE  2.26.
TYPICAL  MRF  CONSTRUCTION  COSTSa)
  ($/sq  ft  FLOOR  AREA)
Item Low
Site Work S3.00




Utilities S1.00


Structures S20.00





General S1 .00
Conditions b)

Contingency c) S2.SO
Total S27.50
High Average Cost Segments
$10.00 S6.50 Excavation
Grading
Paving
Landscaping
Weigh Scale
S2.00 S1.SO Electrical
Water
Sewage
S40.00 S30.00 Concrete
Structural
Doors
Indoor Utilities
Fire Control
Lighting
S3.00 S2.00 Bonds
Building Permit
Mobilization
SS.SO $4.00
S60.SO S44.00
          a) Excludes engineering fee. See Table 2-29.
          b) Equal to 5% of other construction costs.
          c) Equal to 10% of other construction costs.
                                  2-73

-------
 TABLE  2.27.   TYPICAL MRF  FLOOR AREA REQUIREMENTS  BY
                  THROUGHPUT  CAPACITY  (Sq.  Ft.)a)
Area Use
Tipping Floor b)
2 Day Capacity
3 Day Capacity
Processing
Storage c)
7 Day Capacity
14 Day Capacity
28 Day Capacity
TOTAL - Low
TOTAL - High
TOTAL - Average
FT2/TPD - Low
FT2/TPD - High
FT2/TPD - Average

10
3,000
3,000
6,000
1,750
3,500
10,750
12,500
11,625
1,075
1,250
1,163
Capacity (TPD)
100
7,500
11,250
20,000
8,750
17,500
36,250
48,750
42,500
363
488
426

500
30,000
45,000
50,000
35,000
115,000
130,000
122,500
230
260
245
a)  Except as noted.

b)  Assumes a density of 300 Ib/cu yd, piled 12 feet high and a maneuvering factor
   of 2.5 for 10 to 100 TPD and 2 for 300 to 500 TPD.

c)  Assumes a processed material density of 800 Ib/cu yd and maneuvering factors equal
   to those for the tipping floor.
                                2-74

-------






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                            2-78

-------
 fee in order to  provide a range of total capital  costs  for each
 throughput capacity.

      The ranges of total capital cost presented herein are at the
 upper end of the cost range for existing facilities.   The reasons
 for this phenomenon are as follows:

           many existing facilities do not have adequate floor area
           for unprocessed and processed material storage;

           many existing facilities  have been  developed  within
           existing  structures,  thereby  avoiding  stringent  new
           building codes; and

           the inclusion of commingled mixed  paper in  the  facility
           designed for this document increases  capital costs for
           both   sorting  area  and  equipment.     Most   existing
           facilities do not have this  capability.

 2.5.4   Operating  Costs

 2.5.4.1  Labor  Requirements—
     A  range of labor requirements based  upon  facility throughput
 capacity  is  presented in Table 2.32.  The data  in  the table show
 that  the  greatest  variability  is  associated with  the   sorting
 function.    Sorting efficiency  (expressed  as  man-hours/ton)  is
 highly  dependent upon each particular facility design.   In  general,
 labor requirements for sorting per ton of material will  decrease
 with increased  capacity,  due to  the  increased  need  for mechanical
 separation   equipment  such  as  classifiers  and  eddy   current
 separators.

     The number of sorters required also depends upon the degree of
 commingling  of  recyclable  categories.    A  MRF which   receives
 separated  material  categories   (e.g.,   clear glass versus  color
 mixed)  will  require   significantly  fewer  sorters   than   those
 indicated in Table  2.32.

 2.5.4.2  Operations  and Maintenance—
     Operations and maintenance (O&M) costs are presented in Tables
 2.33 and 2.34  Of the O&M cost elements listed in the  tables  the
 costs that will vary the greatest include:   (l) heating (which  is
 a  strong  function  of  geographical   location  and   degree   of
 insulation);  (2)  maintenance  (which  is a function of type and
 quality  of  the  equipment  as  well  as  diligence   of  routine
maintenance); and  (3) residue disposal.

     Debt service has been included based upon  an interest rate of
 10-s _ amortized over 20 years  for facilities  and seven years for
equipment.  Taxes  and  depreciation have not  been included in the
tables  due  to  their dependence on  plant location and  the tax
structure of each  particular business and financial  arrangement.

                               2-79

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          TABLE  2.32.    TYPICAL  MRF  LABOR  REQUIREMENTS

Manager
Foreman/Operator
Sorters
Maintenance
Other a)
Administrative b)
TOTAL
Manhours/TPD Low
Manhours/TPD High
Manhours/TPD Average
10
1
1
1-2
0-1
0
0
3-6
2.4
4.8
3.6
Capacity (TPO)
100
1
1-2
13-25
1-2
4-5
1-2
21-37
1.7
3.0
2.3
500
1
3-4
60-80
4
10-12
2-3
80-104
1.3
1.7
1.5
                    a)  Includes rolling stock operators, equipment monitors and cleanup staff.
                    b)  Includes scale monitors, bookkeepers and clerical staff.


TABLE  2.33.    TYPICAL  MRF UNIT  OPERATING  AND MAINTENANCE
                      COSTS
                        Cost Item
                                                 Units
                                                                       S/Unit
                LABOR
                 Sorters
                 Other

                OVERHEAD b)

                MAINTENANCE


                INSURANCE c)

                UTIUT1ES
                 Power
                 Water & Sewage
                 Heating d)
                 FUEL

                 OUTSIDE SERVICES
                  & SUPPLIES

                 RESIDUE DISPOSAL
(a)
(a)

40% Labor
15 KWH/Ton (Low)
20 KWH/Ton (High)

70 GPD/Person
0 MBTU/Ton (Low)
0.05 MBTU/Ton (High)

0.2 Gal/Ton

10% Operating Costs


0.1 Ton/Ton
$6.00/Hour
$12.00/Hour
$2.00/Ton (Low)
$2.50/Ton (High)

$3.00/Ton (Low)
$4.00/Ton (High)

0.04 $/KWH (Low)
0.07 $/KWH (High)

$2.00/1000 Gal
$4.00 $/MBTU (Low)
$8.00 $/MBTU (High)

$1.20/Gal
$25.00 $/Ton (Low)
$100.00 $/Ton (High)
                  a) Varies based on number of employees per Ton. See Table 2-30.
                  b) Includes Social Security, vacation and sick leave and insurance.
                  c) Includes workers' compensation, property and liabilty.
                  d) Range of use based on climatic extremes.
                                           2-80

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                                               2-81

-------
Consequently, the costs as presented may be considered appropriate
for a publicly  owned  and  operated MRF.

2.5.5   Sensitivity  Of Capital And Operating Costs

     As previously  indicated,  the  capital and  operating costs
presented herein are based upon a recyclables stream which  includes
mixed waste  paper  (MWP) and  old corrugated containers  (OCC).  The
cost of sorting OCC and MWP from newspaper is  substantial.   If the
list of recyclable  materials is altered to eliminate MWP  and OCC,
the specifications  for a  given MRF  capacity  would be reduced as
follows:

          total floor area and construction capital costs  would be
          reduced by  30%;

          total sorting system costs would be  reduced by  50%; and

          sorting labor effort and costs  (including overhead) would
          be reduced  by 50%.

The .total impact on annual costs (including debt service)  would be
a  reduction  of  over 30% when compared to  costs included  in Table
2.34.

2.6  PERFORMANCE GUARANTEES

     Performance guarantees  are established by the contractor, and
normally  become  a  part  of the  Agreement.   The  contractor is
required to  meet the guarantees presented throughout the course of
the operating period.

2.6.1   Facility Availability

     A  contractor  might guarantee,  for example, that the  MRF and
its processing  system would be capable of operating for 16 hrs per
day  for 6 days per week, if necessary.   Any exceptions  to this
blanket guarantee should  be  incorporated in the Agreement.

'2.6.2   Facility Capacity

     Guarantees on  the capabilities of the processing system are
required.  An example of  specified  coverage is as  follows.

2.6.2.1  Paper Processing System—
     A  guaranteed  rated capacity,  TPD,  for newspaper,  corrugated
cardboard,  office  paper,  and  mixed paper would be established.
Also,   a  guaranteed  maximum process  residue  per ton  of paper
processed would be given.   (Note:   the process residue  maximums
cannot  be practically guaranteed unless the collection system is
properly managed.)
                               2-82

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 2.6.2.2  Commingled Processing System—
      A guaranteed  rated capacity,  TPD,  for  commingled  material
 (paper excluded)  would be established.  Also, a guaranteed maximum
 process residue per ton of commingled material would be given.

      Guarantees would  be made that material specifications would be
 met.   These specifications would include glass,  aluminum,  ferrous
 and plastics;  specifications would be detailed in the Agreement.

 2.6.3  Environmental Guarantee

      The  contractor would  guarantee that all components of  the
 facility  would comply  with  all  applicable  federal  and  state
 ordinances,  rules  and regulations,  and any  federal,  state,  or
 county permits, licenses,  or approvals issued  with respect to the
 facility.

 2.7  MARKETING

      It is  readily  apparent to anyone in the recycling  field that
 stable markets for collected materials are vital to any  successful
 program.    The recycling  movement  has  increased  in  popularity
 throughout  the United States; however,  it has brought with  it a
 need  to ensure that once materials are collected there will  be a
 market for  them.    Skeptics  of  any waste  management practices
 utilizing recycling will habitually ask the question," what  happens
 if  you lose your market?"    (In  fact,  this is  a very important
 question; established  secure markets are vital to any  successful
 MRF operation.)  This attitude also prevails in the political  arena
 where states or municipalities who are committed to recycling  major
 portions of the solid waste stream are asking these same questions
 regarding the  disposition of  the  recycled material.

      An encouraging factor for the future of recycling is the  rapid
 rise  in waste disposal  costs over the last few years throughout the
 country.  This  "avoided cost"  situation has  favorably altered the
 economics of recycling; however, much of the  industry will  survive
 only  if the  revenue  from  the sale  of  recyclable  materials is
 sufficient.  (It should be  noted that there  is some  indication of
 declining costs for  disposal  in some areas  of  the country due to
 source reduction, recycling, recession, etc.  diverting waste from
 landfills and  incinerators, and creating  "shortages of waste.")

 2.7.1  Market Concerns for Recovered Wastepaper

     At the  present time,  the waste paper  market is one  of the
recycling industry's primary concerns.  Over the past year or two
the industry has blamed successful residential curbside collection
programs for causing a glut in the market place,  and a subsequent
recession in the waste paper markets.
                              2-83

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     The waste paper markets have experienced dramatic downturns in
the past; these downturns  occurred  in  the  early 70s and again in
the early 80s.   Therefore, the industry has experienced ups and
downs  long  before  residential   collection programs  were  ever
instituted.   (Government supported residential collection programs
were essentially nonexistent in the  70s and early 80s.)  Yet today
some industry representatives are blaming local governments for the
potential demise of the waste paper  business.  However, most large
city governments have no choice but to develop aggressive recycling
programs as a means of  reducing operational costs, extend landfill
life, and reduce the environmental hazards of landfilling.

     Newsprint manufacturers are  now receiving pressure from their
customers to  use more  and  more recycled newsprint;  this pressure
may  result  in  additional production of  newsprint  containing
recycled fiber.  In another paper arena,  capacity is growing for
the use of old corrugated cardboard  (OCC).   The  utilization of OCC
at the  manufacturing mills now exceeds a  million  tons  per year.
The  trend  for OCC  use is  positive;  it has  grown  at a  rate of
12 percent per year over  the  past  several  years.   In  addition,
recycling of high-grade office  paper  has  grown  at a rate  of 4
1/2 percent per year over the last  10 years.  Mixed paper markets
show less promise;  also, decreases in packaging  (source reduction)
may take away some mixed paper markets.   A compilation of waste
recovery figures for 1989 and 1990  is shown  in  Table 2.35.

     It does appear that markets  for recyclable  paper products are
adjusting to this  supply increase  that will allow  more and more
citizens to participate in waste  reduction.  Markets in the United
States in the past  have responded to the public demand for consumer
products, and hopefully will respond to the public desire  to reduce
waste and purchase  recycled products.

2.7.2  Market Concerns  for Recovered Steel  Containers

     A  ready market exists for steel  cans.   When discussing the
recycling of steel  cans,  reference  is  made to two types of cans:
 (1)  the common  tin can  (tin plated)  that  is widely  used for
foodstuffs,  etc.;   and  (2) the  bimetallic  can (steel  can  with
aluminum  top) that is used  for carbonated beverages.    A most
important  point to remember  is that  steel scrap has  been an
essential ingredient in steel making for some time.  In  fact, the
process is designed to utilize steel scrap, so that  the market for
steel  cans  should  continue to be  dependable and  very  likely an
expanding one.

     As  is  found with  other secondary commodity materials, steel
can  prices  will vary  according  to market demand and geographic
region.   Because  of  the  world   wide  market demand,  prices for
established  grades  of iron and steel scrap  are published  regularly
in a number  of national publications.   For example, steel can
                               2-84

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      TABLE 2.35.   WASTE PAPER RECOVERY FIGURES
News
Corrugated
Mixed
High Grades

  TOTAL
                          1990 Waste Paper Data
                             (000 Short Tons)

                      Consumption at U.S.
                     Paper and Paperboard
                     	Mills*
 4,679.2
10,447.7
 2,491.9
 4.761.7

22,380.5
                                              6,504.9
   Total
 Collected

  5,935.9
 13,178.5
  3,638.2
  6.132.8

 28,885.4
News
Corrugated
Mixed
High Grades

  TOTAL
                          1989 Waste Paper Data
                             (000  Short  Tons)

                      Consumption  at U.S.
                     Paper and Paperboard
                     	  Mills*
 4,138.1
 9,993.5
 2,355.6
 4.455.1
                          20,942.3
                  6,307.0
  Total
Collected

 5,419.2
12,912.3
 3,209.3
 5.708.5

27,249.3
  Includes  consumption  of molded pulp and other nonpaper uses.
  (American Paper  Institute)
                                2-85

-------
prices for baled railcar quantities are published in the scrap iron
and steel prices section of American Metal Market and in Iron Age.

     Markets for all recycled  materials  including  steel  cans are
essentially regional in nature. The Steel Can Recycling Institute
(SCRI) maintains an up-to-date  list of known purchasers throughout
the  country for  steel.    This  information  base  is  constantly
expanded as new community programs come on-line.  It is important
then to contact SCRI directly to get the most current information
on scrap steel prices.

     Generally speaking,  the buyers in closest geographic proximity
to a community will be the most logical purchasers of steel cans.
An exception to this general rule is the large national detinning
companies  which have  their own transportation  networks,  and are
presently working to establish regional buying networks for steel
cans.  Establishment of this highly cost effective transportation
system allows communities to market their steel cans to plants that
are hundreds of miles away  from them.

     Steel mills are prime marketers  for  steel cans, but there are
other big potential markets including detinning companies.  These
detinning companies have been working for a long time in recycling
tin cans.  (Direct purchases by steel mills are impacting detinning
economics.)  Iron and steel  foundries are also part of the nation's
steel-making infrastructure. They have not historically used a lot
of steel cans, but the  forecast indicates that this type of market
for recovering steel cans will  be an active one in the years ahead.
Scrap processors and dealers are other potential markets for steel
cans.  They have been  supplying the industry with scrap material
for many years, and their role on scrap recycling and utilizing the
cans is one that looks as if it will increase in the future.

2.7.2.1  Steel Mills as Ultimate Market  for Steel Cans—
     Steel mills are the major  users for most steel cans; there are
more than 120 steel mills in the United States that have operating
furnaces.  The steel-making process allows a certain amount of tin
in the  scrap mix;   also,  mills can combine steel can  scrap with
other scrap sources to produce new steel.  The  steel industry has
been  recycling scrap  steel heavily  through the  80s;  in fact,
approximately  100 billion pounds of used steel  were remelted each
year in the 80s.

     Steel-mills have essentially two types of  furnaces:   (1) the
basic  oxygen  furnace which utilizes  approximately  20-30 percent
recycled steel  scrap, and  (2)  the electric arc  furnace which uses
nearly 100 percent scrap.  As time goes on,  steel cans are becoming
more and more  an essential  part of the scrap mix.

     In  preparing   steel  cans  for market,  the method  used will
depend pretty  much on  the  end market.   For  example,  cans can be
shipped  loose,  shredded,  or baled loosely  or densely.   Also, the

                               2-86

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 end markets do not necessarily need to receive cans with labels and
 ends  removed;  and  steel  mills are  generally tolerant  of small
 levels  of foreign  matter.    Paper  labels  and small amounts  of
 plastic found on the tops  of aerosol containers, for instance, are
 burned in the extremely high temperatures  of the furnace, so there
 is really no  need  for concern for contamination from this material.
 Bimetal cans, also do not  require any special preparation for sale
 to steel mills.  They should be  collected  and processed mixed with
 all other types of steel cans; in fact, the aluminum found on the
 tops  of  steel beverage cans actually  enhance the steel  makincr
 process.                                                        ^

 2.7.2.2  Detinning Companies as Ultimate Market for Steel Cans—
      In addition to  the steel mills, detinners also purchase steel
 cans directly.   Most  of  them  have sophisticated equipment  that
 shreds the cans so that paper labels  and other minor contaminants
 are  removed  prior  to  detinning.    Through  various processes
 detinners remove  the tin  from  steel  products containing  steel'
 Then they sell the detinned steel to steel  mills and foundries,  and
 the recovered  tin to  its  appropriate  markets.   Each steel  can
 purchaser whether it be a steel company,  a foundry,  a  detinning
 company,  or whatever,  has  its own specifications  for postconsumer
 steel cans.   In  each category, the steel can scrap  may  include
 aluminum  lids,  but  generally  excludes  nonmetallics  or other
 nonferrous metals, except  those used  in can  construction.

 2-7.3  Market Concerns  for Recovered Glass

      There are  a number of ways glass  bottles can  be  reused.  They
 can be ingredients  in  the making of fiber  glass and reflective
 beading;  they have  also been  used to  help  control beach front
 erosion and as a  substitute for stone in the making of roadway
 glasphalt."   However,  the  most logical  market  for  used glass
 containers is a glass  plant similar  to the  one  where they were
 manufactured.  At a glass plant they can be melted  down and remade
 as new bottles and jars  in a true example of closed-loop recycling
 Nearly  all   plants  purchase glass  from  the  general  public;
 therefore, for any beginning recycling project a glass plant  is the
 ideal spot to sell bottles  and jars.   For those who are not near a
 glass plant,  a call to  one of the many  intermediate glass brokers
 would  be  in order.   When  contacting  the  plant or broker  it is
 advisable to determine the  hours of operation, prices  paid, and any
 particular  quality  requirements.   Most  plants  will  provide  a
 specification sheet upon request.

     If a recycler has substantial tonnage of  cullet (broken glass)
 to sell, he may be referred  to  the  company recycling director to
make  special  arrangements.   An investigation  of  the market will
 show_   that    glass    recycling   specifications    are    rather
 straightforward.  It is most  important that the material  be color
sorted and contaminant free.  The question then might arise  what
 is color sorted?  For example, would a load of green glass be

                              2-87

-------
rejected if it has one  amber  container?   Also,  just what are the
contaminants that are of concern.

     Color sorting is truly essential to the operation of a glass
plant;  because  it  is  most  important  to  assure  that  newly
manufactured containers match the color specifications required by
the customer.  For example, if too much amber glass is put into a
clear flint batch, it can result in off-color bottles.  Further,
mixed color cullet can cause chemical  composition problems; it can
interfere with the redness ratio  which controls light transmission
through a container.  With large amounts  of contaminants, reactions
between the reducing and oxidizing agents  found in brown and green
glass can create foaming in a melting  furnace.  Nevertheless, some
markets do exist  for mixed color cullet,  especially in the fiber
glass industry.  However, those markets are neither as stable nor
as lucrative  as  those for  color  sorted glass.   Occasionally one
hears talk of an "ecology"  bottle; it is made entirely from mixed
color cullet,  but such  a  container  finds  few buyers in today's
market place.

     There   is   some    tolerance   in   color  separation;   and
specifications will vary from plant to plant.  However, in general
to process glass into furnace-ready cullet  so that  it can be used
directly in the manufacture of new glass  containers  (bear in mind
that  these  guidelines   are not  necessarily  acceptable  for  all
consumers):

     •  only  container  glass  is  acceptable;

        glass must be separated by color into  flint  (clear), amber
         (brown), and green;

        in  flint glass, only 5 percent of  the  total load can be
        colors other than flint; in amber glass  10 percent; and in
        green glass  up  to  20  percent;

        glass must be free  of any refractory materials;  it will be
        rejected if  there is more than a trivial amount of ceramic
        material;  and

        glass must be free of metallic fragments and objects, dirt,
        excessive amounts of paper, or large amounts of excessively
        decorated  glass.

     As  previously  stated,  there  is  an  excellent market   for
contaminant  free cullet; however, practically no market  exists  for
contaminated cullet.  Some of the contaminants that most  effect  a
glass plant  operation are metal caps and lids, ceramics,  stones,
and dirt.  In the making of new glass containers,  silica sand, soda
ash, and limestone are the  primary raw ingredients.   Cullet can be
added  to  this mixture,  which   is  then  heated  to  approximately
2600"F.   At this temperature the batch mixture is turned into  a

                               2-88

-------
  fiery molten  state that  can be  formed into  bottles and  jars-
  however   metals,  ceramics,  and stones  do not melt.   Instead  thev
  remain intact  and can  damage  the  glass melting  furnacS? or appear
  xn the new containers that are being made.  Ceramics are especially
  bad  because  they may breakup into countless  fragments;  and,  ?hey
  are  not  usually  found  until  they  show  up in  the  newly  made
  containers     These imperfections  would  normally Se  Saught  by
  inspection before they leave the plant; however,  at this point they
  have  already created a major  manufacturing problem.
 thai-  ;i             °f contamination is the ceramic and wire caps
 that  are found on  some  beer and  wine bottles.   since the cans
 remain attached to the neck of the bottle, they often end up in ?he
 recycling bin, and, subsequently at the glass plant.  Most  o? thS
 ?h^°£:?ig aSS Pla^S haVS beneficiation units on site, or nearby
 laSelT   KemOVe ™^1 contaminants, as well as plastic and paper
 labels.   However,  these  units  won't detect ceramics  or  stones
 Thus, a .solution ^ to this potential problem must depend on Sa?2?Si
                    SUPPlier  of  the  cullet.   Although  paper and
                    not need to be removed, the  bottles should be
 sor'H     S-f  rUle  °f thUmb'  a bottle  clean e*°U9h to bl
 stored in a home while awaiting collection should be clean enough
 to be  recycled.   On  another note,  it  is  well  to be  aware that
 r"™?^? g^ass  is "hat  the glass plants need and want    Heat
 resistant glass,  along with windshields,  windows, and  crystal
 should never be mixed with bottles  and jars  as  their ingredients
 are different,  and the glass plants do not want  them.  ingredlents
 ™  HK  plants do not require  that  glass bottles and  jars  be
 crushed by recyclers.   The  main reason  for crushing by a recycle?

 TLre^ore111^  TT* f°r- Iff"  ±n handli^ *nd  transportation!
 Therefore  the  question  might arise  as  to  whether a  beginning
 recycler should  invest in a glass  crusher.  The answer would defend
 to JeCu?n^U?  a%th.t V°,1Ume exPected'  ^e type of transport J£n
 to be  utilized,  and  the distance  to the market.  Usually if glass

 crush  theSal?rd "M bUlk in  dUmP trUCkS'  ^ is not  necessary To
 crush  the glass.  Many recyclers  ship  glass in "gaylord"  boxes-

 foTa  lo^S!C??  h°ld ^ mUCh  aS a  t0n °f CUllet' a^d  are desJgnJd
 usSa?iv «5 ^  KI °perat^on-  However, for high volume  users,  it  is
 usually advisable to ship by  dump  truck, or even by rail.

     The  future  of the glass cullet market  looks  promising.  At
 present,  usage is estimated to be 25 to 30 percent;  however  the
 inf I*** ^ ann°unced an ove^H  goal of 50 percent cuSlet Ssage
 a?d has ;etup glass recycling  programs over much  of the United
 70+*™    Y Pi    C°Uld increase their c^Het  consumption to the
 70 to 75 percent range,  if there were adequate supplies of cullet
 stable6 f°£eseeable  future'  c«Het pricesshould SmaJn ?flaSvely
materials  a^^h106  °f  CUl1^  reflects  the  avoided  cost  of raw
materials, and the energy savings for the lower melting temperature
?radUeSde of a4f'    ^^  aluminum'  glas= Bullet is  not  Actively
traded  on  the  world  markets;  so,  does  not  fluctuate due  to
                               2-89

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international  demand or  currency  rates.    Perhaps  the  biggest
question is, can  recyclers  provide  the quantity of quality color
sorted  glass  that  the  plants  need?   Curbside   programs  that
commingle material are bound to produce some glass residue that can
not be  color sorted.  Glass  container plants will be unable to
accept this residue  and alternative markets must be pursued.

2.7.4  Market Concerns for Recovered Aluminum

     The recycling in the United States of aluminum used beverage
cans  (UBCs)  continues  to  increase.   This  trend is shown  in
Table 2.36,   where  the  1990   recycling   rate   is  _ listed  as
63.6 percent.   Further,  this  translates  to a  recycling  of 54.9
billion  cans,  with  the  recovery of some  1.93  billion pounds of
aluminum.  As shown  in Table 2.36,  aluminum UBC  recycling has been
increasing  dramatically  for several years, especially during the
1980s.
          TABLE 2.36.  U.S. ALUMINUM UBC RECYCLING RATES
               Year
                      Million Lbs.
                                  Billion Cans
                                              Recvcling %
1972 53 1-2
1980 609 14.8
1985 1,245 33.1
1989 1,688 49.4
1990 1,934 54.9
Calculation for 1991 rate:
UBC scrap (billion Ibs.)
Average number of cans/1 b.
Total cans recycled (billions)
Total new cans shipped (billions)
Recycling rate
(Aluminum Assn., Can Manufacturers Insti
of Scrap Recycling Industries)
15.4
37.3
51 .0
60.8
63.6

1 .934
28.43
54.984
86.513
63.6


     Most  of this recovered aluminum has gone  directly back into
 new cans  because it is possible to make an aluminum can entirely
 of recycled metal.  Typically,  an  aluminum can body is made from
 used aluminum beverage cans and  can manufacturing scrap.  However,
 primary aluminum  (from the  ore)  is needed as the  total  volume
 demand considerably exceeds the supply of recycled metal.  Aluminum
 can ends are typically made from alloyed primary aluminum and end
 manufacturing scrap.  Therefore, it is possible to have a finished
 aluminum  can and  end that  come  almost  entirely  from  recycled
 sources.   It  is likely,  however, that  the  newly manufactured
 aluminum can will be produced from  a mixture of  recycled aluminum,
 can manufacturing  scrap  and  primary  aluminum  in   percentages
 dictated  by  company  needs,  production   schedules   and  market
 economics at the time.

                                2-90

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                remember, however, is that every aluminum can that
            targ° int° a ^SW °an-  This situation assures a never
                     con^ainer  that  d°es have the best  recycling
           the.beverage  industry.   Further,  aluminum produced  by
 i   fro^reqUireS 95 Percent less ^ergy than that needed to make
 it  from the ore.   This contributes to  a  scrap value that  makes
 recycling  possible  without  any kind   of  corporate  subsTidv  o?

 tnTc^V;SlStanSe-   N° °ther bevera^e Container materYalY has
 the capability,  as  does aluminum, to pay the public a sufficient
 amount  of^money to motivate them  to  recycle.  The value  if t£e~?f
 the market is there; aluminum can recycling will work.     rnere'

     All major  beer  brands and  most  soft  drinks  are  sold  in
 aluminum  cans;   about  95 percent  of today's  beverage  CMS are
 aluminum.  In addition,  most cans are clearly  labeledfas?recyclable
           ^'tt^ can be verified by placing a magneton thS
 e clean and  dr-                t0 aluminum) -  Aluminum cans  must
be clean and  dry for recycling,  or most  recycling  centers  win
deduct 10 percent from the purchase price for dirty or wet
containers.  Further,  it is well to remember to keep the collected
cans  in a  secure place,  indoors if  possible.    Use!  cans art
                                       P   a  vehicle^o3 wind
                             2-91

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                             SECTION  3

                        GENERAL MRF CONCERNS

 3 . 1  SITING AND PERMITTING CONCERNS
 Plr^eVnJ\111Cri.^ia "eed  t0  be considered when  locating a MRF.
 First of all, it is desirable that the MRF be near the collection
 area, since minimization of travel  distances  is  quite  important to
 the successful operation of a MRF.  In addition to  proximity to thS
 collection routes, access to major haul routes  is also important
 Access roads  must be able  to  handle heavy  truck traffic; also"
 truck routes should be designed to minimize the impact  of vehicular
 ?«5    £n  .surjoundin?  neighborhoods.    Aside  from  the  routing
 tS*  ?' '  ?S    d °n WhlGh the MRF is  to be built must  be zoned fS?
 }2o?S?ia  P£rp°seS'  *nd the area Used should P^vide  satisfactory
 isolation.   Further,  it  is most important when siting a facility to
 involve  the neighborhood, and secure community  acceptance.   mils
 is, ^n many cases, the most difficult  task in the siting procedure"
 Of interest  is the fact that some communities have had  good success
 in using closed landfill sites  as sites for new MRFs .      success

    In  the  past,  the  decision-making  process  for  situations
 concerning   municipal   solid   waste   management   was   normally
 centralized  in  the hands  of  a  few  key  governmental pe?sonSel
 However,  over the_ last  20 years  or so,  nongovernmental Pin?e£ests
 have  become  more involved in local  decision-making; and,  citizSJ
 have  demonstrated that  they will not accept "behind  the  scenes?
 wh?^10^ °V     waste ^nagement.   Therefore,  the manner  in
 which the siting  process is carried out  for  a MRF  can have a
 thpnini??nt  SMftCt  °nn PUbl±C accePtance  of the overall project  by
 waste tJiJT* „       Y °an-a closed-d°°r,  decision-making  process
 waste time and resources, it can jeopardize the credibility of the
      8}??  plaTrs'  *«rther,  if the trust and confidence of the
       is lost,  it  is nearly impossible to recover.
               pr°ces!s. normally consists of three related phases:
  v  nf*         selection and facility design, and implementation.
t"L°   th^6  StageS  °f the Sitin5  Process may be subjected to
intense public comment and debate.  A review of the  major steps in
facility siting  (EPA/530-SW-90-019) show that important decision^
are  made  very  early in  the planning  phase for  a  solid  wast!
management facility  (Figure 3-1) .                      fuj-J-a  wasre
to d^^mTn^16' T17 ln thS Plannin
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Phase 1:  Planning"
  Identifying the Problem
  Designing the Siting Strategy
  Assessing Alternatives
• Choosing Site Feasibility Criteria
Recognizing the growing waste stream, rising
costs, and capacity shortfall.
Planning and integrating public involvement,
risk communication, mitigation, and evaluation
activities.
Researching, debating, and choosing among the
options: recycling, source reduction, incineration
and land disposal.
Studying population densities, hydro-
geological conditions, and socioeconomic
characteristics.
 Phase II: Site Selection and Facility Design
 « Selecting the Site
 • Designing the Facility
 Performing initial site screening and
 designation; acquiring land; conducting permit
 procedures; developing environmental
 impact statements.
 Choosing technologies, dimensions, safety
 characteristics, restrictions, mitigation plans,
 compensation arrangements, and construction.
 Phase III: Implementation
   Operation
   Management
 • Closure and Future Land Uses
 Monitoring incoming waste; managing waste
 disposal; performing visual and lab testing;
 controlling noise, litter, and odor.
 Monitoring operations and safety features;
 performing random testing of waste; enforcing
 permit conditions.
 Closing and securing the facility; deciding on
 future land uses; and performing continued
 monitoring.
   Figure  3-1.   The three-phase siting framework
                                     3-2

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facility that is really needed.  Later, after a decision has been
made to site a MRF, a major issue remains  as to  its  location.  The
criteria that are assessed to determine suitability for a potential
site    include    hydrogeological    conditions,    socioeconomic
characteristics, and population densities.  Regardless of where the
MRF is located,  the  burden of  the facility will be placed on the
people living nearby; thus, exposing them to more noise, traffic,
and pollution than  the  overall population being  served  by the
facility.  Sometimes  these constituencies are rural or  impoverished
people  who  tend to  be  poorly represented  in  the  traditional
decision-making process.   Nevertheless, these people  can gain the
support of a large coalition from within or outside the community
in response to potential  inequities or other political issues.

    In  selecting  a site  for  a MRF,   some  citizens  will  almost
certainly question the validity of any technical work  carried out.
Also,   the  involved  community   will be concerned  about  negative
effects on property values,  safety, air quality,  noise, and litter;
or about broader issues such as the impact on community prestige.
Some citizens may argue  for compensation  arrangements,  or other
forms of guarantees against negative impacts.  Also,  it is normal
for  public   opposition   to increase  as  site  selection  time
approaches.   Finally,  before   a  site  is  selected,  the  overall
project  must be  approved  by  state  agencies     that are  often
responsive to political pressure from community groups.

    The public concerns are usually associated with safety features
of the facility.  Groundwater contamination and air pollution are
by  far the issues most frequently  requiring attention,  although
noise,  litter,  and traffic  issues  also appear.   The operator's
credentials and past  record are also important concerns during site
selection  or facility design.   Other  points  of  contention may
include the types  of  wastes allowed at the site,  and whether the
site should be restricted to local haulers.

    Operation and management plans for  a MRF  often are  important to
the general  public.    Demands  are  sometimes  made  for  strict
monitoring  and  enforcement  activities to  ensure  compliance  by
haulers and operators. These demands may include local supervision
of the facility, along with state  agencies'  support of the local
enforcement efforts.   These actions may include revoking disposal
permits,  testing wastes, and monitoring air and groundwater.  It is
also important to note that no  siting proposal is complete without
planning for  closure  and  future land use.   Local  citizenry will
often argue  how the  land should be  used  after closure,  or how
groundwater monitoring should be maintained.

    Issues and challenges facing public officials and citizens have
changed over the last  two decades.  It  is reasonable to expect that
new issues  and  new challenges  will emerge in the  coming  years.
There  is  no set  of  procedural  steps that  will  guarantee  a
successful  siting process.    Public  officials  from  different

                               3-3

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communities  must  tailer  their  siting  strategy  to  their  own
particular needs  and issues.   The following guidelines summarize
the most important points made in this discussion:

    •   accept the public as a legitimate partner;
    •   listen to the  concerns of the different interests and groups
       in the community;
    •   plan a  siting process that permits  full  consideration of
       policy alternatives;
    •   set goals  and objectives  for public  involvement  and risk
       communication activities in each step of the process;
    •   create  mechanisms  for  involving  the  public  early  in
       decision-making process;
    •   provide  risk  information  that  the  public needs  to  make
       informed decisions;
    •   be prepared to mitigate negative impacts on the community;
       and
    •   evaluate the  effectiveness of public involvement  and risk
       communication activities.

   Although these eight guidelines are not all-encompassing, each
is  important  in  defining an  effective  siting  process.    The
guidelines are specific enough to lend  structure  to a multitude of
planning  activities, but  they do  not  substitute for the  good
judgement of project leaders and other interested parties.

3.2  CONTRACTING ISSUES

   Unlike  air and water pollution control which has been largely
regulated at the state and federal levels, solid,waste disposal has
traditionally   been  the  responsibility  of  local  governments
(although now  regulated, to a degree,  at both state  and federal
levels).  However, the design,  construction  and operation of a MRF
is more  like  a general business enterprise  than are the  more
traditional municipal functions,  such as  public health and safety,
social services, etc. Nevertheless, there are now a growing number
of private/public partnerships in the MRF industry that illustrate
the utilization of  the resources and  capabilities of a  public
agency,  while  enjoying the greater  flexibility  and  efficiency
associated with private sector operations.

   When a local government  undertakes establishing a MRF as a means
of reducing the solid waste disposal stream, it must first assess
its own capabilities and then  define the role .of any prospective
private partner.  Conversely, however, it may be in the interest of
a private developer to attempt to  interest a public agency in such
an endeavor.   In any event,  promoters of any kind  of  recycling
initiatives  often  have  to  abide  by  public  procurement  and
contracting procedures that have been dictated by state and local
law.
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 3.2.1  Contractual Arrangements

    Before entering into any type of MRF  contractual  arrangement,
 the sponsor of such a  program  must address certain  issues:   (l)
 what recyclable materials are actually  present in the waste stream,
 and their quantities;  (2)  is the processing facility going  to  be
 directed toward centralized mechanical processing or more toward
 source  separation;  and (3)  what  is  the  relationship  with the
 markets,  and  the  quantity  and quality  of  recovered materials that
 can be  sold.

   _ A successful recycling  project will often involve  some form  of
 joint venture between a public agency and a private contractor.
 Among the MRFs which are currently operational, approximately  65
 percent are owned by private firms with  the remaining facilities
 owned  by the  public  or  not-for-profit  sectors   (GAA,   1990).
 However,  with  regard  to  the  planned  facilities,  the  ownership
 picture changes substantially; 62 percent  of the planned facilities
 will  be publicly  owned, with  the  private  sector  decreasing its
 share to  38 percent of  the projects.   However,  despite this  trend
 toward  public ownership and financing,  private firms will continue
 to  operate most of these facilities.   Private enterprises  operate
 83  percent  of  the existing  projects,  and about  the  same (79
 percent)  of planned  installations   (GAA, 1990).   A  more recent
 survey  (Biocycle,  1991) showed a reversal in this trend with  about
 73 percent of all operating facilities  being privately owned, with
 82  percent being privately operated.

    A formal procurement aimed  at establishing a MRF  can  involve:
 (1) either  a  two-step  process,  where  responses to  a  request for
 qualifications  (RFQ)  are evaluated to  establish a  short list of
 qualified contractors who are eligible  to respond to a request for
 proposal  (RFP),  or (2)  a combined  RFQ/RFP  under which  each firm
 making a proposal has to establish its qualifications in the course
 of extending its offer.   Whether contractors are screened first in
 an  RFQ  or  as  part  of  an RFP,  the  importance  of  selecting  a
 qualified party can not be  overemphasized.  There is no substitute
 for  a contractor having the appropriate  skills,  experience, and
 technical   and   financial   resources   to  implement   a   project
 effectively.  In order  to  give  an idea of the scope  of  an RFP,  a
 sample Table of Contents for an RFP is  shown in Table 3.1.

    The  RFP  should present  as  much  background  information  as
 possible concerning the project; any contractor before submitting
 a response to an RFP will want to know that the proposed facility
 has a good chance of being financed and built.  The background
 section of  the RFP should  include  a  discussion  of   a number of
 topics.    For example, the  RFP should address the  demographic and
 economic  characteristics  of  the area,   legal  authority  of  the
procuring agency, the type of guarantee with regard to  the waste
 supply,  information concerning any private recycling programs that
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               TABLE 3.1.  SAMPLE TABLE OF CONTENTS FOR AN RFP
                           (TO RECEIVE, PROCESS,  AND MARKET
                           HOUSEHOLD RECYCLABLE MATERIALS)
                                   CONTENTS
1   General Information

    1.1   Introduction
    1.2   Plan Implementation
    1.3   Overall Program Timing

2  Project Overview

    2.1   Introduction
    2.2   Recycling Implementation Plan
    2.3   Procurement of MRF Services
    2.4   Recyclable Materials Collection and Delivery
    2.5   Recyclable Materials Quality
    2.6   Recyclable Materials Quantities
    2.7   General Requirements

3  Technical Requirements

    3.1   Facility Requirements
    3.2   Operations Requirements
    3.3   Environmental Performance Standards
    3.4   MRF Public Education Facility Requirements
    3.5   Proposer Technical Experience and Qualifications

4  Service Requirements and Business Arrangements

    4.1   General
    4.2   Service Requirements for Facility Siting, Permitting,
           Design, and Construction
    4.3   Service Requirements for Facility Operations
    4.4   Option to Provide Services to Private Customers
    4.5   Term of Service
    4.6   Performance Guarantees and Assurances
    4.7   Financing
    4.8   Performance Bonds and Proposal Security
    4.9   Payment for Services
    4.10  Business Proposal
    4.11  Default and Remedies
    4.12  Insurance Requirements
    4.13  Other Requirements
    4.14  Minimum Financial Qualifications
    4.15  City Policy Compliance

                                                          (continued)
                                     3-6

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                           TABLE 3.1.   (continued)
5  Proposal Requirements and Evaluation

    5.1   Executive Summary
    5.2   Qualifications of Proposer and Project Organization
    5.3   Technical Proposal
    5.4   Business Proposal
    5.5   City Policy Compliance
    5.6   Proposal Evaluation Criteria

APPENDICES

Appendix A  Historical Daily Tonnages (FY 1987-88)
Appendix B  Technical  and Business Proposal Forms
Appendix C  City Policy and Compliance Attachments
                                     3-7

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are taking place in this area,  and what sort of public support and
regulatory requirements are to be expected.

   Next, the RFP should detail the respective responsibilities of
the procuring agency and the contractor.   Normally the municipality
would be involved  in furnishing  the  facility  site,  and providing
information  necessary for  securing  any types of  environmental
permits  for construction  and operation of the  facility.   The
municipality would also usually be responsible for delivering, or
having delivered,  the recyclable material to the  facility.   The
municipality probably would  also be in  a  position  of exercising
legal control over  the disposal  of waste materials  from the MRF.
Further, a typical RFP will normally assign to the contractor any
risks and  responsibilities  involved  in developing  the project.
These responsibilities can include design  and  construction,  and
furnishing of the labor,  supplies, materials, equipment, services,
and technology  necessary to complete the  facility  in accordance
with product specifications.

   The RFP should contain a section dealing with the criteria under
which the proposals  will  be  evaluated.   Points that are normally
covered  in  the criteria  include the  following:    (1)  technical
feasibility of the facility design;  (2) prior experience with this
design,  and whether  or not similar  facilities  have been operated
elsewhere;  (3)  qualifications of the  personnel assigned  to  the
project;  (4)  efficiency and reliability of the proposed system,
with special attention to the subjects of safety and environmental
protection;  (5)  credit  rating  and  financial  stability  of  the
proposing party;  and  (6)  net  revenue  or net cost that would be
imposed on the procuring agency.

   Although the RFP and the resultant proposal tend to be lengthy,
complex documents, the end result is an  offer  by the proposer to
the public  agency  to perform certain work  for  a  specified price
under terms  and conditions  established  in the  RFP.   (A  sample
proposal Table of Contents is shown in Table 3.2.)  Further, it is
certain that an effective public/private sector partnership depends
on a clear understanding by each party of its respective  rights and
obligations.

3.2.2  Flow Control

   Municipalities are now being forced  to resort to waste disposal
methods other than landfilling.  This has come about largely due to
the shortage of  landfill capacity in the United States.  Recycling,
composting, and other types of approaches to municipal waste stream
management are being explored extensively.  When considering a MRF,
it is essential  that the municipality be able to guarantee delivery
of consistent amounts of solid waste.  This  can be accomplished by
a municipality only if it can control the waste  streams within its
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              TABLE  3.2.   SAMPLE  TABLE OF CONTENTS FOR A PROPOSAL
                         SAMPLE  ELEMENTS OF A PROPOSAL
                 PROPOSER QUALIFICATIONS, TECHNICAL PROPOSAL
                   BUSINESS PROPOSAL, CITY POLICY COMPLIANCE
                                   CONTENTS

Section I—Proposer Qualifications

1.0  Introduction

1.1  Project Team Experience

     1.1.1  Design and Technical Qualifications
     1.1.2  Reference Facility

1.2  Project Team Organization

     1.2.1  Organizational Chart
     1.2.2  Design/Equip Team
     1.2.3  Operations Management
     1.2.4  Project Team Staffing

1.3  Local Employment Opportunities, Local Business Involvement

1.4  Financial Qualifications

1.5  Personnel and Facility Management

1.6  Marketing Management

1.7  Technical Ability

Section II—Technical  Proposal

2.0  Introduction

2.1  Location

2.2  General  Design

     2.2.1  Building Description

                                                        (continued)
                                     3-9

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                           TABLE 3.2.  (continued)
            2.2.1.1  Architecture
            2.2.1.2  Building Description
            2.2.1.3  Public Education Facility Description
            2.2.1.4  Building Structures, Utilities, and Details

     2.2.2  Tipping Hall
     2.2.3  Commingled Recyclables Line
     2.2.4  Breakage Minimization and Broken Glass Recovery
     2.2.5  Paper Processing Line
     2.2.6  Material Stockpiling and Storage

2.3  Operating Plan

     2.3.1  Facility Scheduling
     2.3.2  Throughput Capacity
     2.3.3  Materials Receipt
     2.3.4  Materials Inspection and Quality Control
     2.3.5  Residue Removal
     2.3.6  Process Residue Allowance
     2.3.7  Unacceptable/Hazardous Waste Procedures
     2.3.8  Records and Reports
     2.3.9  Secondary Materials Marketing Schedule

2.4  Maintenance Plan

     2.4.1  General Maintenance
     2.4.2  Site Maintenance—"Good Neighbor Provision"
     2.4.3  Equipment Maintenance

2.5  Onsite Traffic Handling

     2.5.1  Municipal Collection Vehicles
     2.5.2  Transfer Trailers
     2.5.3  Employee and Visitor Vehicles

2.6  Personnel

     2.6.1  MRF Staff
     2.6.2  Job Descriptions
     2.6.3  Employee Training
     2.6.4  Health and Safety Plan
     2.6.5  Job Partnership Training Act (JPTA)
     2.6.6  Contract Labor

                                                        (continued)
                                     3-10

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                           TABLE 3.2.   (continued)
2.7  Permitting Plan.

2.8  Utilities

2.9  Other Facility Users

2.10 Multiple Proposals/Combined Facilities

2.11 Environmental Impact Assessment

2.12 Process Flow Diagram

2.13 Process Control and Instrumentation

2.14 Process Mass Balance

2.15 Process Energy and Water Balance

2.16 Availability Analysis

     2.16.1  System Availability
     2.16.2  Rugged Engineering
     2.16.3  Built-in Surge Capacity
     2.16.4  Contingency Sorting and Processing Strategies

2.17 System Capacity

     2.17.1  Expanding Minimum Design Capacity—Mixed Recyclables
     2.17.2  Expanding Minimum Design Capacity—Paper Line
     2.17.3  Expanding Minimum Design Capacity—2 Shift Operation

2.18 Product Specification:

     Glass, Aluminum, Tin, PET, HOPE

2.19 Materials Marketing:

     Aluminum, PET, HOPE, Tin, Glass, Mixed Gullet, Newspaper,
     Letters of Intent

Facility Drawings and Schedules                                      ,

     Site Plan Layout
     General Arrangement
     Facility Cross Section
     Electrical Single-Line Diagram
     Schedule

                                                           (continued)
                                     3-11

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                           TABLE 3.2.  (continued)
Technical Proposal Forms
     B-2   Technical Description of Site/Facility/Equipment
     B-ll  Performance Guarantees
     B-12  Performance Assurances
     B-13  Product Specifications
Section III—Business Proposal
     Proposal Forms
Section IV—City Policy Compliance
4.0  Contractor's Past Record
4.1  Construction Phase Compliance
4.2  Local Employment Opportunities
4.3  Operations Phase Compliance
4.4  Non-Profit Organization Involvement
Appendices
Appendix A:  Resumes of Key Project Team Members
Appendix B:  Throughput Verification and Material Storage Calculations
List of Tables
Table 1:  Contractor's Recycling Facilities
Table 2:  Project Organization Chart
Table 3:  Operations Staffing Chart
Table 4:  Facility Throughput Capacities
Table 5:  Processed Material Loadout Chart
Table 6:  Facility Staffing
Table 7:  Potential  Future Recyclable Materials
Table 8:  Revenue Projections
                                     3-12

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boundaries.  It is normal practice, however, that a municipality in
controlling the MSW stream within its boundaries controls both  the
disposal site of  the waste and the price paid  for  disposal.

    Municipalities typically exercise control  over waste flow  by
passing legislation that  requires haulers to transport  the solid
waste they have collected to a disposal  site that is determined by
the municipality.  The haulers  pay a tipping fee  at the disposal
site;  the  fee  is  established  by  the  municipality.    However,
competitive concerns may be raised because this legislation, passed
by  the municipality,  might  allow the municipality  to essentially
control the entire market for solid  waste disposal.  Accordingly,
activities of this type could come within the jurisdiction of  the
federal  antitrust laws.    State  and  local  governments, simply
because  they are governmental  entities,  are  not  automatically
exempt from federal antitrust laws.  In addition,  private parties
that contract with such governmental entities for  waste  disposal
services are also potentially liable  under  federal  antitrust laws.

    Now while state governments may be exempt,  municipal governments
do  not necessarily receive  a blanket exemption because  they have
only delegated, not sovereign power.  However, the United States
Supreme Court has ruled that municipalities qualify for  the state
action  exemption  so  long as  their  anticompetitive  behavior   is
undertaken  pursuant  to  a  clearly  articulated   state  policy.
Further,  protection  from  antitrust damage  liability   is  also
available under the Local Government Antitrust Act  of 1984, which
prohibits damage  actions  against  local government officials and
employees acting in an  official capacity as well as  private persons
acting at government direction.

    Once  it  has been determined  that it is  legal  to control the
waste stream, the next step  is to determine how this control is to
be exercised.  A municipality does have a variety of options with
regard to controlling the waste  stream.   First,  control can  be
exercised merely  by requiring its  drivers  to haul  the waste to a
specific site.  Second, the municipality might have  a contract with
the haulers  which would  authorize them to  haul the waste  to a
specific  site.    Or  thirdly,  the municipality could  authorize
private collection by allowing a  direct  contractual arrangement
between the residents and the private haulers.

    Another area where the municipality must retain  control is the
cost of  disposal.  The municipality would typically  develop  an
annual rate  setting  procedure  based on  estimated cost of  the
disposal system and estimated revenues from the system.  This rate
determination procedure would normally be administered by  an agency
that has been given the authority to manage the solid waste system.

    Waste flow control  to a MRF is necessary not only for financial
reasons,  but in order for the system to operate efficiently.  A MRF
would be developed to handle  a specific level  of throughput.   If

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that level of waste is not available, costly downtime results for
the facility.  An insufficient amount of waste also would increase
the cost per ton of waste handled,  and would  have a detrimental
effect  on  equipment  maintenance schedules.   It  is clear  that
municipal  control  over the  waste  stream  is essential  to  an
efficient waste disposal system and the lack of  control can lead to
unintended  consequences.    If  waste flow  control  and  proper
administration is carried out, then the municipality will better be
able to ensure  that  its  waste  disposal  system  can operate  as
anticipated.
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               APPENDIX A

                Glossary

  (Definitions  drawn principally from
ASTM Special Technical Publication 832,
          H.I.  Hollander,  ed.)
                  A-l

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                       List of Descriptions
Acceptance testing
Aggregate
Air classification
Air classifier
Air dry
Air knife
Testing of process equipment and
the overall processing system.

A granular material of mineral
composition such as sand, gravel,
shell, slag, or crushed stone used
with a cementing medium to form
mortars or concrete, or alone as in
base courses, railroad ballasts,
etc.

A process in which a stream of air
is used to separate mixed material
according to the size, density, and
aerodynamic drag of the pieces.

A mechanical device using air
currents to separate solid
components into "light-fraction" or
"heavy-fraction."

Paper or paperboard is air dry when
its moisture content is in
equilibrium with atmospheric
conditions to which it is exposed.
According to trade custom air dry
pulps are assumed to contain 10%
moisture, and are sold on this
basis.

Jargon for a blower device intended
to separate steel cans from more
massive pieces or iron and steel.
Angle of repose
ANSI
APC
The maximum acute angle that the
inclined surface of a pile of
loosely divided material naturally
makes with the horizontal.

American National Standards
Institute.

Air Pollution Control.
                               A-2

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 Apron conveyor
Ash
Baler
Ballistic separator
Baffle
Bond paper
Bridge crane


Briquetter
Broker
 A set of continuous chains that are
 supported and moved by a system of
 sprockets and rollers while
 carrying overlapping or
 interlocking plates upon which bulk
 materials are moved.

 The inert residue  that remains
 after a  solid waste and fuel
 mixture  has  been incinerated.

 A machine used to  compress
 recyclables  into bundles to reduce
 volume.   Balers are often used on
 newspaper, plastics,  and corrugated
 cardboard.

 A device that drops mixed materials
 having different physical
 characteristics onto  a high-speed
 rotary impeller; they are hurled
 off at different velocities and
 land in  separate bins.

 A construction used to close or
 deflect  the  delivery  of a moving
 substance.

 Term originally meant  paper used
 for printing  bonds  and stocks,  now
 generally refers to high  grade
 papers used  for letters  and high
 quality  printed work.   It  is
 surface-sized  for better  writing
 and  printing  quality.

 A  lifting unit  that can maneuver
 horizontally  in two directions.

 A machine that  compresses a
 material, such  as metal turnings,
 coal dust, or RDF (refuse derived
 fuel), into objects, usually shaped
 like a pill,  pellet, or pillow.

An individual or group of
 individuals that acts as an agent
or intermediary between the sellers
and buyers of recyclable materials.
                               A-3

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Buffer zone
Bulk density



Bulky waste
Buy-back center
By-products
Capacity factor
Clamshell bucket
Neutral area which acts as a
protective barrier separating two
conflicting forces.  An area which
acts to minimize the impact of
pollutants on the environment or
public welfare.  For example, a
buffer zone is established between
a composting facility and
neighboring residents to minimize
odor problems.

The weight in air of a volume of
material including voids normal to
the material.

Large items of refuse including,
but not limited to, appliances,
furniture; large auto parts;
nonhazardous construction and
demolition materials; and trees,
branches, and stumps which cannot
be handled by normal solid waste
processing, collection, and
disposal methods.

A facility where individuals bring
recyclables in exchange for
payment.

Materials which result from
operation of a facility and which
cannot be composted; but which can,
within reason, be recycled,
marketed, processed, or otherwise
utilized.

The ratio of the average load on a
machine or equipment for the period
of time considered, to the capacity
rating of the machine or equipment.

A vessel used with a hoist to
convey materials; it has two jaws
that clamp together when the vessel
is lifted by specially attached
cables.
                               A-4

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 Clean Air Act
 Clean Water Act
Commercial waste
Commingled recyclables


Comminution

Compaction
Compactor
 Act passed by Congress to have the
 air "safe enough to protect the
 public's health."  Requires the
 setting of National Ambient Air
 Quality Standards (NAAQS)  for major
 primary air pollutants.

 Act passed by Congress to protect
 the nation's water resources.
 Requires the EPA to establish a
 system of national effluent
 standards for major water
 pollutants,  requires all
 municipalities to use secondary
 sewage treatment,  sets interim
 goals  of making all U.S.  waters
 safe for fishing and swimming,
 allows point source discharges of
 pollutants into waterways  only with
 a  permit from the EPA, requires all
 industries to use the best
 practicable  technology (BPT)  for
 control of conventional  and
 nonconventional pollutants,  and to
 use the best available technology
 (BAT)  that is reasonable or
 affordable.

 Waste  materials originating in
 wholesale, retail,  institutional,
 or  service establishments  such  as
 office buildings,  stores,  markets,
 theaters,  hotels,  and warehouses.

 A mixture  of  several  recyclable
 materials.

 Size reduction.

 Compressing wastes to reduce their
 volume.  Compaction allows  for more
 efficient transport, but may reduce
 aeration.

 Power-driven device used to
 compress materials to a smaller
volume.
                               A-5

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Computer printout paper
Container deposit
legislation
Contaminant

Corrugated paper




Gullet



Curbside collection
Cyclone separator
Dense media separation
 Densification  equipment
Consists of white sulfite or
sulfate papers in forms
manufactured for use in data
processing machines.  This grade
may contain colored stripes and/or
computer printing, and may contain
not more than 5% of groundwood in
the packing.  A stock must be
untreated and uncoated.

Laws that reguire monetary deposits
to be levied on beverage
containers.  The money is returned
to the consumer when the containers
are returned to the retailer.  Also
called "Bottle Bills."

Undesirable constituent.

Paper or cardboard manufactured in
a series of wrinkles or folds, or
into alternating ridges and
grooves.

Clean, generally color-sorted,
crushed glass used to make new
glass products.

Programs where recyclable materials
are collected at the curb, often
from special containers, to be
brought to various processing
facilities.

A cylindrical and conical structure
without moving parts, which
utilizes centrifugal force to
remove solids entrained in an air
stream.

A separation process of nonferrous
metal from  other  large particles
such as rubber, plastic, bone, or
leather, using a  fluid solution
with a specific gravity about twice
that of water.  The metal fraction
sinks in the solution while  other
material floats.

Balers, pellet mills, briguetters,
cubetters,  etc.
                                A-6

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 Densified refuse-derived
 fuel (d-RDF)
 Density
 Design capacity
 Detinning
 Diversion  rate
Drag conveyor
Drop-off center
Dry process
Dust
 A refuse-derived fuel that has been
 processed to produce briquettes,
 pellets, or cubes.

 The mass divided by the volume at a
 stated temperature.

 The quantity of material that a
 designer anticipates his system
 will be able to process in a
 specified time period under
 specified conditions.

 Recovering tin from "tin" cans by a
 chemical process which makes the
 remaining steel more easily
 recycled.

 A measure of the amount of waste
 materials being diverted for
 recycling compared with the total
 amount that was previously
 discarded.

 A conveyor that uses a series  of
 mechanical  barriers such as steel
 bars  fastened between two
 continuous  chains  to drag material
 along a smooth surface.

 A method of collecting recyclable
 or compostable materials in which
 the materials  are taken  by
 individuals  to collection sites  and
 deposited  into designated
 containers.

 Processes which handle or process
 solid waste  directly  as  received
 without  the  addition  of  water.

 A  loose  term applied  to  solid
 particles predominantly  larger than
 colloidal and capable of temporary
 suspension in air or  other gases.
 Dusts do not tend to  flocculate
 except under electrostatic forces;
 they do not diffuse but settle
under the influence of gravity.
                               A-7

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Dust loading
Eddy current separator
Effluent
Electronic-optical sorter
Electrostatic precipitator
Emission


Energy recovery
An engineering term for "dust
concentration"—among others,
usually applied to the contents of
air or gas ducts and emissions from
stacks, expressed in grains per
cubic foot or pounds per thousand
pounds of gas or other equivalent
units.

A device which passes a varying
magnetic field through feed
material, thereby inducing eddy
currents in the nonferrous metals
present in the feed.  The eddy
currents counteract the magnetic
field and exert a repelling force
on the metals, separating them from
the field and the remainder of the
feed.

Any solid, liquid, or gas which
enters the environment as a
by-product of a man-oriented
process.  The substances that flow
out of a designated source.

Separates glass from stones and
pieces of ceramics; sorts the glass
according to color.  Photoelectric
detector determines the color or
opacity of the material and blasts
of air deflect the pieces into the
proper containers.

Device for removing particulate
matter from MWC facility air
emissions.  It works by causing the
particles to become
electrostatically charged and then
attracting them to an oppositely
charged plate, where they are
precipitated out of the air.

Discharge of a gas into atmospheric
circulation.

Conversion of waste energy,
generally through the combustion of
processed or raw refuse to produce
steam.  See also Municipal Waste
Combustion and Incineration.
                               A-8

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 Enterprise fund
 EPA
 Feedstock
 Ferrous metals
 Fines
 Finished products




 Firm capacity



 Flail



 Flat glass



Flight conveyor



Flint glass
 A fund for a specific purpose that
 is self-supporting from the revenue
 it generates.

 (United States) Environmental
 Protection Agency.

 Waste material furnished to a
 machine or process.

 Predominantly iron and steel
 materials (typically contains small
 amounts of paper,  textiles,
 plastic,  and nonferrous metals)  -
 can be recovered by magnetic
 separation.

 Very short pulp fibers or fiber
 fragments escape during paper
 forming in the process water;  may
 be recovered for reuse or go into
 sludges.   Waste paper processing
 creates extensive  fines.

 Wood  chips,  manure,  screened
 compost,  and other products
 produced  from Acceptable  Yard
 Debris.

 Assumed facility processing
 capacity  accounting  for equipment
 vulnerability.

 A metal flange  or  tine attached  to
 a rotating shaft for moving,
 mixing, and aerating leaves.

 A general term  covering sheet
 glass, plate glass, and various
 forms of rolled glass.

A drag conveyor that has rollers
 interspersed in its pull chains to
reduce friction.

A lead-containing colorless glass.
                               A-9

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Flow control
Fly ash
Front-end loader
Front-end recovery
Froth flotation
Grade
Gravity separation
A legal or economic means by which
waste is directed to particular
destinations.  For example, an
ordinance requiring that certain
wastes be sent to a combustion
facility is waste flow control.

Small, solid particles of ash and
soot generated when coal, oil, or
waste materials are burned.  Fly
ash is suspended in the flue gas
after combustion and is removed by
the pollution control equipment.

A tractor vehicle with a
bucket-type loader at the front end
of the vehicle.

Mechanical processing of as-
discarded solid wastes into
separate constituents.

A process for separating, in
aqueous suspension, finely divided
particles that have different
surface characteristics.  Reagents
are selected which, when added to
the mixture, will coat only the
desired material and make their
surfaces water-repellent
(hydrophobic).  When air is bubbled
through the solution, the coated
particles become affixed to the air
bubbles and are buoyed to the
surface where they can be removed
as froth.

A term applied to a paper or pulp
which is ranked  (or distinguished
from other papers or pulps) on the
basis of its use, appearance,
quality, manufacturing history, raw
materials, performance, or a
combination of these factors.

Concentration or separation of a
mix of materials based on
differences  in specific gravity and
sizes of materials.
                               A-10

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Hammer-mill
HOPE
 Ground wood pulp              A wood pulp  produced mechanically
                               by a  grinding  action that separates
                               wood  fibers  from resinous binders.
                               It is used principally  for
                               newsprint and  printing  papers.

                               A type of crusher or shredder used
                               to break up  waste materials  into.
                               smaller pieces.

                               High-density polyethylene
                               containers (containers  for milk,
                               liquid detergents, bleach, film,
                               cosmetics, and medicines).

                               Separation of  solids  into heavy and
                               light fractions  in a  fluid medium
                               whose density  lies between the
                               fractions.

                               Dense metals,  specifically cadmium,
                               mercury, lead, copper,  silver,
                               zinc,  and chromium, which may be
                               found in the waste stream.  High
                               concentrations in  compost can
                               restrict use.

                               Household hazardous waste.

                              Relatively valuable types  of paper
                               such  as computer printout, white
                               ledger, and tab cards.  Also used
                              to refer to industrial trimmings at
                              paper mills that are recycled.

Horsepower, shaft             Actual horsepower produced by an
(flywheel or belt horsepower)  engine, after deducting the drag of
                              accessories.
Heavy media separation
Heavy metals
HHW

High-grade paper
Inclined plate conveyor
                              A separating device that operates
                              by feeding material onto an
                              inclined steel plate backed belt
                              conveyor so that heavy and
                              resilient materials, such as glass,
                              bounce down the conveyor, and light
                              and inelastic materials are carried
                              upward by the motion of the belt.
                              A-ll

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Inertial separator
Inorganic waste
Institutional waste
Integrated solid
waste management
Intermediate processing
center  (IPC)
IPC

IRB

Kraft paper
LDPE
Device that relies on ballistic or
gravity separation of materials
having different physical
characteristics.

Waste composed of matter other than
plant or animal (i.e., contains no
carbon).

Waste materials originating in
schools,  hospitals, prisons,
research institutions, and other
public buildings.

A practice of using several
alternative waste management
techniques to manage and dispose of
specific components of the
municipal solid waste stream.
Waste management alternatives
include source reduction,
recycling, composting, energy
recovery, and landfilling.

Usually refers to the type of
MRF that processes residentially
collected mixed recyclables into
new products available for market;
often used interchangeably with
MRF.

See intermediate processing center.

Industrial revenue bond.

A paper made predominantly from
wood pulp produced by a modified
sulfate pulping process.  It is a
comparatively coarse paper
particularly noted for its
strength, and in unbleached grades
is used primarily as a wrapper or
packaging material.

Low-density polyethylene  containers
 (trash bags, diaper backing, fruit
and vegetable self-serve  bags,
storage bags).
                               A-12

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 Lignin
 Live bottom bin
 Live bottom pit
 Magnetic fraction
Magnetic  separation
Magnetic separator



Mandatory recycling
Manual separation
Mass burn
 An amorphous polymeric substance
 related to cellulose that, together
 with cellulose, forms the woody
 cell walls of plants and the
 cementing material between them.

 A storage bin for shredded or
 granular material whereby
 controlled discharge is by a
 mechanical or vibrating device
 across the bin bottom.

 A storage pit,  usually rectangular,
 receiving truck unloaded material,
 utilizing a push platen or
 bulkhead,  reciprocating rams or
 mechanical conveyor across the pit
 floor for controlled discharge
 (retrieval)  of  the material.

 The portion of  municipal  ferrous
 scrap remaining after the
 nonmagnetic contaminants  have been
 manually removed and the  magnetic
 fraction washed with water and
 dried at ambient temperature  or as
 required by ASTM C29.

 A  system to remove ferrous  metals
 from  other materials in a mixed
 municipal  waste stream.   Magnets
 are used to  attract  the ferrous
 metals.

 A  device available in several
 forms, used to  remove iron  and
 steel from a stream  of material.

 Programs which by  law require
 consumers  to separate trash so  that
 some or  all recyclable materials
 are not burned or  dumped  in
 landfills.

The separation of  recyclable or
compostable materials from waste by
hand sorting.

Combustion of solid waste without
preprocessing,  as  in a mass burn
incinerator.
                              A-13

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Material balance




Material specification



Mechanical collector




Mechanical separation




Mixed MSW


Mixed paper




Monorail crane



MRF

MSW

NAAQS


NESHAP


New  corrugated  cuttings
An accounting of the weights of
material entering and leaving a
process usually made on a time
related basis.

Stipulates the character of certain
materials to meet the necessary
performance requirements.

A device that separates entrained
dust from gas through the
application of inertial and
gravitational forces.

The separation of waste into
various components using mechanical
means, such as cyclones, trommels,
and vibrating screens.

MSW that has not undergone source
separation.

Low-grade recyclable paper
 (paperboard, books, catalogs,
construction paper, glossy coated
paper  (except magazines).

A lifting unit, suspended from  a
single rail, that can only move in
one horizontal direction.

Materials Recovery  Facility.

Municipal Solid Waste.

National Ambient Air Quality
 Standards.

 National Emission Standards  for
 Hazardous Air Pollutants.

 Consists of  baled corrugated
 cuttings having two or  more  liners
 of  either jute or Kraft.
 Nonsoluble adhesives, butt  rolls,
 slabbed  or hogged medium, and
 treated  medium or liners are  not
 acceptable  in this  grade.
                               A-14

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 Newsprint
 NIMBY
 Noncompostable
 Nonferrous metal


 NRC



 NRHW

 NSPS
NSWMA


OBW

OCC

ONP

Organic waste
 A  generic term used  to  describe
 paper  of the type generally used  in
 the publication of newspapers.  The
 furnish is largely mechanical wood
 pulp,  along with some chemical wood
 pulp.

 Acronym of "Not In My Back Yard"  -
 expression of resident  opposition
 to the siting of a solid waste
 facility based on the particular
 location proposed.

 Incapable of decomposing naturally
 or of yielding safe,  nontoxic end
 products.   Noncompostable materials
 include glass,  batteries, cans,
 etc.

 Any metal  other than  iron and its
 alloys.

 National Recycling Coalition;  now
 called RAG  (Recycling Advisory
 Council).

 Nonregulated hazardous waste.

 New Source Performance Standards  -
 EPA's  rule which requires the
 removal of 25% of the waste stream
 as  the  best available control
 technology (BACT) for WTE plants.

 National Solid Waste  Management
 Association.

 Oversize bulky waste.

 Old corrugated cardboard.

 Old newspapers.

 Waste material containing
 carbon-to-carbon bonds and being
 biodegradable.   The organic
 fraction of municipal  solid waste
 includes paper,  wood,  food wastes,
plastics,  and yard wastes.
                              A-15

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Particle
Particle size
Performance bond
Performance specification
Performance test
 PET
 Picking table or belt
 Post-consumer recycling
A small, discrete mass of solid or
liquid matter, including aerosols,
dusts, fumes, mists, smokes, and
sprays.

An expression of the size of liquid
or solid particles expressed as the
average or equivalent diameter or
minimum of two linear dimensions.

A bond or other instrument
guaranteeing the performance of all
obligations of the proposer or
guarantor to acquire and construct
a facility.

States the desired operation or
function of a product or process
but does not specify the materials
from  which the product must be
constructed.

A test  devised to permit rigorous
observation  and measurement of the
performance  of a unit of equipment
or a  system  under prescribed
operating conditions.

Polyethylene terepthalate
 (carbonated  soft drink  bottles)
 (beverage containers  redeemable
under the California  bottle bill,
AB  2020).

Table or belt on which  solid  waste
 is  manually  sorted  and  certain
 items are  removed.   Normally  used
 in  composting and materials salvage
 operations.

 The reuse  of materials  generated
 from residential  and commercial
 waste,  excluding recycling of
 materials  from industrial  processes
 that has not reached the consumer,
 such as glass broken in the
 manufacturing process.
                                A-16

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 Post-consumer waste
 PP




 Primary materials




 PS


 PSD


 Pulverization



 PVC


 RAG



 Rated capacity



RCRA


Recovery
 Material or product that has  served
 its  intended use and has been
 discarded for disposal after
 passing through the hands of  a
 final user.  Part of the broader
 category, "recycled material."

 Polypropylene (syrup bottles,
 yogurt and margarine tubs, shampoo
 containers, container caps and
 lids, drinking straws).

 Virgin or new materials used  for
 manufacturing basic products.
 Examples include wood pulp,  iron
 ore,  and silica sand.

 Polystyrene (disposable dishes,
 cups, bowls,  egg cartons).

 Prevention  of significant
 deterioration.

 The crushing  or  grinding  of
 materials into very  fine  particle
 size.

 Polyvinyl chloride  (meat  wrap,
 bottles  for edible oils).

 Recycling Advisory Council;
 formerly NRC  (National Recycling
 Coalition).

 The quantity of material that  the
 system can process under
 demonstrated test conditions.

 Resource Conservation and Recovery
 Act.                             *

 The process of retrieving materials
 or energy resources from wastes.
Also referred to as extraction,
reclamation,  recycling,  and
salvage.
                              A-17

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Recyclables
Recycling
Refuse
Refuse Derived  Fuel  (RDF)
 Residential  waste


 Residue
 Residue conveyor
 Resource recovery
Materials that still have useful
physical or chemical properties
after serving their original
purpose and that can, therefore, be
reused or remanufactured into
additional products.

The process by which materials
otherwise destined for disposal are
collected, reprocessed or
remanufactured, and reused.

Putrescible and nonputrescible
solid wastes, except body wastes,
and including kitchen discards,
rubbish, ashes, incinerator ash,
incinerator residue, street
cleanings, and market, commercial,
office, and industrial wastes.

Boiler  fuel made by  shredding and
screening solid waste into a
material of relatively uniform
handling and combustion  properties.
Often,  recyclables  can be recovered
from the RDF process.

Waste materials generated in  single
and multiple-family homes.

Materials remaining after
processing,  incineration,
composting,  or  recycling have been
completed.   Residues are usually
disposed  of  in  landfills.

A conveyor,  usually of  the  drag or
 flight  type,  used  to remove
 incinerator  residue from a  quench
 trough  to a  discharge point.

 A term  describing  the extraction
 and utilization of materials  and
 energy  from  the waste stream.  The
 term is sometimes  used  synonymously
 with energy  recovery.
                                A-18

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 Reuse
 RFP

 Roll-off container




 Rotary screen




 Scavenger



 Scrap



 Screen
Screening
Screw conveyor
Secondary material
 The use of a product more than once
 in its same form for the same
 purpose; e.g., a soft drink bottle
 is reused when it is returned to
 the bottling company for refilling.

 Request For Proposal.

 A large waste container that fits
 onto a tractor trailer that can be
 dropped off and picked up
 hydraulically.

 An inclined meshed cylinder that
 rotates on its axis and screens
 material places in its upper end.
 Also known as trommel.

 One who removes materials at any
 point in the solid waste management
 system.

 Discarded or rejected industrial
 waste material often suitable for
 recycling.

 A  surface provided with apertures
 of uniform size.   A machine
 provided with  one  or more screening
 surfaces to separate materials  by
 size.

 The process of passing  compost
 through  a  screen or  sieve to  remove
 large  organic  or inorganic
 materials  and  improve the
 consistency and quality of the
 end-product.

 A  rotating  shaft with a continuous
 helical  flight to move granular
 type material, along a trough or
 tube.

A material that is used in place of
a primary or raw material in
manufacturing a product.
                              A-19

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Shear shredder
Shredder
Size-reduction equipment

Solid waste
Source reduction
Source separation
Special waste
Stack emissions
A size reduction machine that cuts
material between large blades or
between a blade and a stationary
edge.  See Grinder, Hammermill,
Shredder.

A mechanical device used to break
up waste materials into smaller
pieces, usually in the form of
irregularly shaped strips.
Shredding devices include tub mill
grinders, hammermills, flail mills,
shears, drum pulverizers, wet
pulpers, and rasp mills.

Hammermills, shredders, etc.

Garbage, refuse, sludge from a
water supply treatment plant or air
contaminant treatment facility, and
other discarded waste materials and
sludges in solid, semi-solid,
liquid, or contained gaseous form,
resulting from industrial,
commercial, mining and agricultural
operations, and from community
activities.

The design, manufacture,
acquisition, and reuse of materials
so as to minimize the quantity
and/or toxicity of waste produced.
Source reduction prevents waste
either by redesigning products or
by otherwise changing societal
patterns of consumption, use, and
waste generation.

The segregation of specific
materials at the point of
generation  for separate collection.
Residences  source  separate
recyclables as part of a curbside
recycling program.

Refers to items that require
special  or  separate handling,  such
as household hazardous wastes,
bulky wastes, tires, and used  oil.

Air  emissions from a combustion
facility's  stacks.
                               A-20

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Storage




Storage pit


Subtitle C



Subtitle D




Subtitle F
SWDA

SWMP

Tin can


Tipping fee
Tipping floor
TPD

TPH

TPW
The  interim containment of solid
waste, in an approved manner, after
generation and prior to ultimate
disposal.  See live bottom bin.

A pit  in which solid waste is held
prior  to processing.

The  hazardous waste section of the
Resource Conservation and Recovery
Act  (RCRA).

The  solid, nonhazardous waste
section of the Resource
Conservation and Recovery Act
(RCRA).

Section of the Resource
Conservation and Recovery Act
(RCRA) requiring the federal
government to actively participate
in procurement programs fostering
the  recovery and use of recycled
materials and energy.

Solid Waste Disposal Act.

Solid waste management plan.

A container made from tin-plated
steel.

A fee, usually dollars per ton, for
the  unloading or dumping of waste
at a landfill,  transfer station,
recycling center, or waste-to-
energy facility,  usually stated in
dollars per ton;  also called a
disposal or service fee.

Unloading area for vehicles that
are delivering municipal solid
waste to a transfer station,
recycling center, composting
facility,  or municipal waste
combustion facility.

Tons per day.

Tons per hour.

Tons per week.
                              A-21

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TPY

Transfer station
Trash
Trommel
Variable container rate




Vibrating screen



Virgin materials
VOC

Volume reduction
Tons per year.

A permanent area where waste
materials are taken from smaller
collection vehicles and placed in
larger vehicles for transport,
including truck trailers, railroad
cars, or barges.  Recycling and
some processing may also take place
at transfer stations.

Material considered worthless,
unnecessary, or offensive that is
usually thrown away.  Generally
defined as dry waste material, but
in common usage it is a synonym for
garbage, rubbish, or refuse.

A perforated rotating essentially
horizontal cylinder  (a hollow
cylindrical screen) used to break
open trash bags, screen large
pieces of glass and remove small
abrasive items such as stones and
dirt.

A charge for solid waste services
based on the volume of waste
generated measured by the number of
containers set out for collection.

An inclined screen that is vibrated
mechanically, and screens material
placed on it.

Material derived from substances
mined, grown, or extracted from
water or the atmosphere, and virgin
materials are juxtaposed to
secondary materials.

Volatile organic compounds.

The processing of waste materials
so as to decrease the amount of
space the materials occupy, usually
by compacting or shredding
(mechanical), incineration
(thermal), or composting
(biological).
                               A-22

-------
 Waste exchange
 Waste paper
 Waste  reduction
Waste  stream
WDF

Wet ton
White goods



WTE

Yield
 A computer and catalog network that
 redirects waste materials back into
 the manufacturing or reuse process
 by matching companies generating
 specific wastes with companies that
 use those wastes as manufacturing
 inputs.

 Any paper or paper product which
 has lost its value for its original
 purpose and has been discarded.
 The term is most commonly used to
 designate paper suitable for
 recycling,  as paper stock.  Paper
 waste generated in the paper
 manufacturing process itself is
 excluded.

 Reducing the amount or type of
 waste generated.   Sometimes used
 synonymously with Source Reduction.

 A  term describing the total flow of
 solid waste from  homes,  businesses,
 institutions,  and manufacturing
 plants that must  be recycled,
 burned,  or  disposed of in
 landfills;  or any segment thereof,
 such  as  the "residential  waste
 stream"  or  the "recyclable waste
 stream."

 Waste  derived fuel  facility.

 Two thousand  pounds  of material,
 "as is."  It  is the  sum of the dry
 weight of the  material, plus its
 moisture content.  Yard waste
 weighed on  truck  scales would
 typically be  reported this way.

 Large household appliances such as
 refrigerators, stoves, air
 conditioners,  and washing machines.

Waste-to-energy.

The guantity or percentage of
recovered product(s) from the
process.
                              A-23

-------

-------
                APPENDIX B




List of Material Grades and Specifications
                   B-l

-------
                 Table 1. Examples of Buyer Specifications for Newspaper

Buyer
A
B
C
D
E
F
Baled
X
X
NO
NO
X
X
Loose
X
X
X
X
—
-
Bundled
_
—
X
X
—
-
Grade
#7
#7
-
#6
-
-
Contamination
Rotogravure
Normal
-
No glossy
—
-
-
Colored
Normal
-
-
-
-
-
occ
-
-
None!
-
-
-

Grocery
Bags
--
-
X
X
-
-

Maximum
Accepted
160TPM
No limit
20-40 TPW
No limit
-
--

Delivery
Trailer
Self -dump
Semi-trailer
Self-dump
Truck/Rail
Flatbed/Van
X = Acceptable

- = Not specified
                Table 2. Examples of Buyer Specifications for OCC

Buyer
A
B
C

Baled
X
X
X
Maximum
Loose Quantity
Accepted
~ —
X No limit
—

Method of
• Delivery
Truck/rail
Self-dump
Flatbed/van
    X = Acceptable
    - = Not specified
                                       B-2

-------
                     Table 3.  Examples of Buyer Specifications for Tin Cans

Buyer
A
B
C
D
Baled Briquet Loose Flattened
70lbs/cuft 70lbs/cuft -
75lbs/cuft - - -
50 Ibs/cu ft X
X - X NO
Contamination
W/Bi-Metal
X
X
--
--
Food
& Labels
X
NO
X
-

Delivery
-
Truck or Rail
truck
Flatbed/Van
X = Acceptable
- = Not specified
                                   GENERAL INFORMATION3
a Cleanness. All grades shall be free of dirt, nonferrous metals, or foreign material of any kind, and
excessive rust and corrosion. However, the terms free of dirt, nonferrous metals, or foreign material of
any kind" are not intended to preclude the accidental inclusion of negligible amounts where it can be
shown that this amount is unavoidable in the customary preparation and handling of the particular orade
involved.                                                               at-       &

b. Off-grade material.  The inclusion in a shipment of a particular grade of iron and steel scrap of a
negligible amount of metallic material which exceeds to a minor extent to meet the applicable
requirements as to quality or kind of material, shall not change the classification of the shipment
provided it can be shown that the inclusion of such off-grade material is unavoidable in the customary
preparation and handling of the grade involved.
1SRI code number

209b
211
213
215
Selected Definitions:

No. 2 bundles. Old black and galvanized steel sheet scrap, hydraulically
compressed to charging box size and weighing not less than 75 Ibs per cu ft. May
not include tin or lead-coated material or vitreous enameled material.

Shredded Scrap. Homogeneous iron and steel scrap magnetically separated,
originating from automobiles, unprepared No. 1 and No. 2 steel, miscellaneous
baling and sheet scrap. Average density 70 Ib/cu ft.

Shredded Tin Cans for Remelting. Shredded steel cans, tin-coated or tin-free
may include aluminum tops but must be free of aluminum cans, nonferrous metals
except those used in can construction, and non-metallics of any kind.

Incinerator bundles. Tin can scrap, compressed to charging box size and
weighing not less than 75 Ibs/cu ft. Processed through a recognized qarbaqe
incinerator.
aAdapted from Scrap Specifications Circular 1990, Institute of Scrap Recycling Industries, Inc. (ISRI).
bCurrent price often used as a basis by buyers for establishing price for tin cans.
                                            B-3

-------
                 Table 4.  Example of Specifications for Aluminum Used Beverage Containers (UBC)'

Density
Ibs/cu ft
Siio




Ferrous
Separation
Ffoo Load
Steal, lead.
bottle caps.
plastic.
cans, olhar
plastics.
glass.
wood, din.
grease.
trash, and
other
foreign
substances
Tying
Method




Skids and/
or support
sheets
Aluminum
hams other
than UBC
Other Hems







Other
Conditions





Shredded
12-17

_




Magnetic

None
None











_





_


Not
acceptable

Including
moisture
by special
arrange-
ment
between
buyer
and seller
Max. of 5%
fines less
than A mesh.
Max. of
2.5% fines
less than
12 mesh.
Dcnsificd
3S-4S

Uniform for a bundle 10'
to 13' X 10'/." to 20' X
6W to 9'
Bundle: 41 'to 44' x 51'
to 54' x 54" to 56- height
Magnetic

None
None











4 to 6 5/8' X 0.020' steel
bands or 6 to 10 #13 ga
steel wires (or aluminum
bands or wires of equiva-
lent strength and
number).
Not acceptable


Not acceptable


Including moisture, by
special arrangement
between buyer and seller





Biscuit shall have band-
ing slots in both
directions to facilitate
banding. One vertical
band per row and min-
imum of two horizontal
bands per bundle.
Baled
14-17 unflattened
22 flattened
3O cu ft minimum.
24' to 40" x 30' to 52'
x 40' to 84'


Magnetic

None
None











4 to 6 S/8' x 0.020' steel
bands or6 to 10 #13
ga steel wires (or alum-
inum bands or wires of
equivalent strength and
number).
Not acceptable


Not acceptable


By special arrangement
between buyer and
seller





_,






Actual Buyer Specifications Baled
14 to 24 -30

30 cu ft minimum 24" to 40' x 30' to 52" x 40" to 72'




_

-
_









.

A minimum of 6 5/8" x 0.020 steel straps or 6 to 1 0
#13 ga steel wires or equivalent are required.
Aluminum bands or wires are acceptable in
equivalent strength and number. Bands or wire of
other material are not acceptable.

Support sheets are not acceptable.


_


Composite bales of two or more individual bales
banded together to meet size specifications are
not acceptable





_






Note: Individual buyers' specifications may differ. Some buyers will accept (and may prefer) UBCs flattened and pneumatically conveyed to transport
     trailers. When buyer provides (lattener/blower at no cost, often a guaranteed monthly volume (e.g.. 25.000 Ibs) is required.

— »  Not specified.
1 Adapted from Scrao Specifications Circular 19SO. Institute of Scrap Recycling Industrie
                                                            B-4

-------
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                                                                        B-5

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                                                             B-6

-------
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w ^_ Q-
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ting paper, and all
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                                       B-7

-------
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anufactured or treated or are in such a form as to be unsuitable for consumption as the grade specified.1
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nnection with the following grade definitions is understood to bo the TOTAL of 'Outlhrows* and 'Prohibitive
o
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CD
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                                         B-£

-------
            APPENDIX C




Examples of Maintenance Procedures
              C-l

-------
                Example of Maintenance Procedures: Belt Conveyor

Item No.                 Description

  1        Drive
    a      Remove debris from motor cooling fins
    b      Check gear case oil level
    c      Check all fasteners and mounting bolts
    d      Check drive belts for tension and wear
    e      Replace guard before running

  2       Head and Tail Pulleys
    a      Remove debris
    b      Lubricate bearings
    c      Check all fasteners and mounting bolts
    d      Check take-up for proper belt tension and belt alignment
    e      Replace guards before running

  3       Idlers                                  .
    a      Remove debris                                 .    .
    b      Lubricate bearings
    c      Check for frozen idlers
    d      Check mounting bolts

  4       Belt
    a      Inspect for damage, wear, and tracking
    b      Check belt splice

  5       Skirting
    a     Remove debris
    b     Check adjustment
    c     Check for damage                 .          .
    d     Check fasteners

  6      Wipers
    a     Remove debris
    b     Check adjustment
    c     Check wear

  7      Controls
    a     Remove debris
    b     Check for damage
    c     Check and adjust emergency shut-off

  8       Comments

Legend: D = Daily;  W = Weekly; M = Monthly; A/R =.As required.
Frequency
    W
    M
    M •
    W
    A/R
    W
    M
    M
    W
    A/R-
     M
     W
     M
     W
     W
     W
     W
     W
     M
     W
     W
     W
     W
     W
     W
                                      C-2

-------
            .    Example of Maintenance Procedures:  Magnetic Separator

  Item No.                Description
    1
     a
     b
     c
     d
     e
     a
     b
     c
     d
     e
     a
     b
     c
     d
     a
     b
     c
     a
     b
     c
     d
    a
    b
 Drive
 Remove debris from motor cooling fins
 Check gear case oil level
 Check all fasteners and mounting bolts
 Check drive belts for tension and wear
 Replace guard before running

 Head and Tail Pulleys
 Remove debris
 Lubricate bearings
 Check all fasteners and mounting bolts
 Check take-up for proper belt tension and belt alignment
 Replace guards before running

 Idlers
 Remove debris
 Lubricate bearings
 Check for frozen idlers
 Check mounting bolts

 Belt
 Inspect for damage, wear, and tracking
 Check belt splice
 Check wear plates and fasteners

 Magnet
 Check oil temperature and oil seepage
 Clean pressure relief valve
 Check oil level
With magnet off, slack off belt and blow away accumulated tramp
 iron from magnet. Re-tighten belt.

Controls
Remove debris
Check for damage

Comments
                                                                         Frequency
 W
 M
 M
 W
 A/R
 W
 M
 M
 W
 A/R
 W
 M
 W
 M
W
W
W
M
M
M
W
W
W
Legend: D = Daily; W - Weekly; M = Monthly; A/R = As required.
                                          C-3

-------
                   Example of Maintenance Procedures: Trommel
Item No.                Description

  1        Drive
    a      Remove debris from motor cooling fins
    b      Check gear case oil level
    c      Check all fasteners and mounting bolts
    d      Lubricate drive shaft couplings
    e      Check drive belts for tension and wear
    f      Check universal joints
    g      Replace guards before running

  2       Trunnions
    a      Check trunnion wheels for wear and alignment
    b      Lubricate trunnion bearings
    c      Check thrust wheels for wear and alignment
    d      Lubricate thrust wheels

  3       Screen
    a     Remove debris from screen openings
    b     Check screen for structural wear or defects

  4      Controls
    a     Remove debris
    b     Check for damage

  5       Comments

Legend: D = Daily; W = Weekly; M = Monthly; A/R = As required.
                                                                       Frequency
W
M
M
M
W
M
A/R
M
M
M
M
 M
 M
 W
 W
                                      C-4

-------
                   Example of Maintenance Procedures:  Can Flattener
  Item No.                 Description

    1        Drives
            Remove debris from motor cooling fins
            Check gear case oil level
            Check all fasteners and mounting bolts

            Conveyor
            Remove debris from head and tail shaft pulleys
            Lubricate bearings
            Check take-up for proper belt tension and alignment
            Check belt for wear and damage
            Check belt splice

            Drum
            Check drum cleats and reverse or replace as required
            Lubricate bearings

            Blower
            Remove debris from intake and blades
            Lubricate bearings

            Controls
            Remove debris
           Check for damage

   6       Comments

Legend: 0 = Daily; W = Weekly; M = Monthly; A/R = As required.
 a
 b
 c
 a
 b
 c
 d
 e
a
b
a
b
a
b
                                                                   Frequency
 W
 M
 M
 W
 M
 W
 W
 W
M
M
W
M
W
W
                                        C-5

-------
                    Example of Maintenance Procedures: Baler

Item No.                Description

  1        Power Unit
    a      Remove debris from motor cooling fins
    b      Check mounting bolts

  2       Hydraulic System
    a      Remove debris from cooler
    b      Check mounting bolts
    c      Check hydraulic oil level
    d      Check for leakage

  3       Wire Rolls
    a      Inspect for quantity and condition

  4       Tie System
    a      Remove debris
    b      Inspect for damage

  5       Shear Knives
    a     Inspect for sharpening and/or replacement

  6      Bale Ejection Chamber
          Remove debris
          Check for damage

          Controls
          Remove debris
          Inspect for damage
          Check and adjust emergency shut-off

   8       Comments

Legend: D = Daily;  W = Weekly; M  = Monthly; A/R = As required.
a
b
a
b
c
                                                                Frequency
                                                                    W
                                                                    M
                                                                     W
                                                                     M
                                                                     M
                                                                     W
                                                                     D
                                                                     D
                                                                     D
                                                                     W
W
W
W
W
W
                                          C-6

-------
BIBLIOGRAPHY
  BB-1

-------
                         BIBLIOGRAPHY
1    Sealy,  G.D., "Magnetic Equipment  for the Scrap Processing
     and Recycling Industries," Recycling Today, August,  1976.

2    Alter  H.,  S.L. Natof, K.L. Woodruff, W.L. Freyberger,  and
     EL  Michaels  "Classification and  Concentration of

     isMiSScrs^i^rir^n^s^s^r
     Mines and IIT Research Institute, Chicago, 1974.

3    Douglas,  E. and P.R. Birch, "Recovery of Potentially
     Reusable  Materials from Domestic Refuse by Physical
     Sorting," Resource Recovery and Conservation, Volume 1, No.
     4, 1976.

4    Twichell, E.S.," Magnetic Separation Equipment  for Municipal
     RefSseT"  Presented at the 104th Annual American Institute of
     MeSanical Engineers Meeting, New York City,  February 17-19,

     1975.

5    Alter  H   S L. Natof, K.L. Woodruff,  and R.D.  Hagen, "The
  '   Recovery'of Magnetic  Metals from Municipal So-^J^e,
     National Center for Resource Recovery,  Inc.,  November, 1977.

 6    Bendersky, D.,  D.R. Keyes, M. Luttrell,  M.  Simister, and D.
     vt£eck? Processing  Equipment  for Resource Recovery Systems,
     Volume I - State of the Art, Municipal Environmental
     Research Laboratory,  U.S.  Environmental  Protection Agency,
     EPA-600/2-80-007a,  Cincinnati, Ohio, July, 198O.

 7    Diaz   L  F., G.M.  Savage,  and  C.G. Golueke, Resource Recovery
     ?rom'Municipal Solid  Waste, Volume I - Primary Processing,
     CRC Press, Boca Raton,  Florida,  1982.

 8.   Abert, J.G., "Aluminum Recovery  - A Status Report",  article
     reprint  from N.C.R.R Bulletin ,  7(2,3),  1977.

 9.   Dalmijn, W.L., W.P.H. Voskuyl,  and H.J. Roorda  "Low-Energy
     Separation of Non-ferrous Metals by Eddy Current
     Techniques," in Recycling Berlin '79, K.J. Thome-Kozmiensky
      (ed.)  Berlin, Germany, 1979.

 10.  Easterbrook, G.E., "Aluminum can't Resist the  Power of the
      Medium," Waste Age, 10(1), 16,  1979.
                               BB-2

-------
 11.
 12,
13
14
15,
16
17
18.
 19.
20.
21.
22.
23.
       Bernheisel, J.R. ,  P.M.  Bagalman,  and  W.S.  Parker,  "Trommel
       Processing of Municipal Solid Waste Prior  to  Shredding"  in
       Proceedings 6th Mineral Waste Utilization  Symposium  U S
       Bureau of Mines and  IIT Research  Institute, Chicago,  May'
       2 — 3 , 1978 .


       Savage, G.M., L.F. Diaz, andG.J. Trezek,  "RDF: Quality  must
       precede Quantity," Waste Age, 9 (4) , 100, 1978 .
     ' qnHw,u    G'J; Trezek' "Screening Shredded Municipal
      Solid Waste," Compost Science, 17(1), 7, 1976.

      Woodruff, K.L., "Preprocessing of Municipal Solid Waste for
      Resource Recovery with a Trommel," in Trans. Soc. Min. Eng
      260, 201, 1976.                                          ^ '

      "j11' ?;M- "Rotary Screens for Solid Waste," Waste Age, 18,
      •3 3 f  x y / / ,

      Sullivan, J.F., Screening Technology Handbook,  Triple/S
      Dynamics, Dallas,  Texas,  1975.                    pj-e/^

      Murray,  D. ,  "Air Classifier Performance and Operating

                 '                                 waste
     Chrisman,  R.L.,  "Air Classification in Resource Recovery "
     National Center for Resource Recovery, Inc.   RM 78-1
     October, 1978.                                       '

     Boettcher  B.A. ,  "Air Classification for Reclamation of
     Solid Wastes,"  Compost Science,  2(6),  22,  1970.

     Fan,  p., "on  the  Air Classified  Light  Fraction of Shredded
     Municipal  Solid Waste - Composition and Physical
                    /" Resource  Recovery and Conservation,  l,
    Savage, G.M., L.F.  Diaz, and G.J. Trezek,  "Performance
    Characteristics of  Air Classifiers  in Resource Recovery
    Processing," in Proceedings of the  1980 National Waste
    Processing Conference, ASME, 1978.

    Ham, R.K. and j.j.  Reinhardt, Final Report on a
    Demonstration Project at Madison Wisconsin to Investigate
    Milling of Solid Wastes Between 1966 and 1972, Volume I
    U.S. Environmental  Protection Agency, March, 1973.     '
                              BB-3

-------
24.  Marshall, V.C., "Crushing and Grinding — Critique of
     Existing Laws," Chemical and Processing Engineering, April,
     1966.

25.  Austin, L.G. and R.R. Klimpel, "Theory of Grinding
     Operations," I and EC Process, Design, and Development,
     56:19-29, 1964.

26.  Snow, R.H., "Annual Review of Size Reduction," Power
     Technology, 5:351-364, 1971-1972.

27.  Bond, F.C., "The Third Theory of Comminution," Trans. AIME,
     193:484-494, 1952.

28.  Trezek, G.J. and G.M. Savage, Significance of Size Reduction
     in Solid Waste Management, EPA-600/2-77-131, Municipal
     Research Laboratory, Office of Research and Development,
     U.S. Environmental Protection Agency, Cincinnati, Ohio
     45268, July, 1977.

29.  Vesiland, P.A., A.E. Rimer, and W.A. Worrell, "Performance
     Characteristics of a Vertical Hammermill Shredder,"  in
     Proceedings 1980 National Waste Processing Conference, ASME,
     May, 1980.

30.  Gaudin, A.M. and T.P. Meloy,  "Model  and a Communition
     Distribution Equation for Single Fracture," Trans. AIME,
     223:40-43,  1962.

31.  Zalosh, R.G.,  et al, Factory  Mutual  Research  Corporation  —
     Assessment  of  Explosion  Hazards  in Refuse Shredders,
     prepared  for the U.S. Energy  Research and Development
     Administration under Contract No.  (49-1)-3737, April,  1976.

32.  Zalosh, R.G. and J.P. Coll, Determination of  Explosion
     Venting Requirements for Municipal Solid Waste Shredders,
     draft  report submitted to the U.S. Environmental  Protection
     Agency,  EPA Contract No. 68-03-2880, September,  1981.

33.  Savage,  G.M.,  D.J.  Lafrenz, D.B. Jones,  and J.C.  Glaub,
     Engineering Design  Manual for Solid  Waste Size Reduction
     Equipment,  U.S. Environmental Protection Agency,  Cincinnati,
     Ohio,  1982.

34.  Governmental Advisory Associates,  Inc.,  "Materials  Recovery
     and Recycling  Yearbook," New  York, New  York,  1990.

35.  J.G. Press,  Inc.,  "Biocycle Guide  to Collecting,  Processing,
     and Marketing  Recyclables," Emmanus, PA,  1990.
                               BB-4

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 37.
U'2'WEPA'  "Sites  for Our Solid  Waste,» Office of Solid Waste

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