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2-19
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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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2-22
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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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2-24
-------
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
-------
Belt
Figure 2-11. Trough type belt conveyor.
Skirtboards
Bolted Adjustable
Rubber Edging
Belt
Figure 2-12.
Belt conveyor with skirtboards.
2-29
-------
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
-------
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
-------
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
-------
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
-------
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
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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.
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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."
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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
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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;
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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
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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.
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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.
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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.
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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.
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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.
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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
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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
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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.
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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
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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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2-77
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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
-------
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
-------
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
-------
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
-------
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
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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
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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
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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.
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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
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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 Phase' choices must be made
to determine a waste management strategy, and whether a MRF is the
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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
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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
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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)
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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
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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)
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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)
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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)
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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
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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
3-13
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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.
3-14
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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.
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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.
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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.
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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).
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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.
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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.
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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.
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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.
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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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-------
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
-------
36.
37.
U'2'WEPA' "Sites for Our Solid Waste,» Office of Solid Waste
March er9enCY ReSP°nSe' Washin
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