; :>l3LIOGn^HIC DATA I I -.--.\ .
j SHEET I EPA/530/SW-^7d.2
PB 234 716
Franklin, Ohio1^
Solid Waste.'and F:
Final Report (Two vc Junes)
ibr-r Recovery Demonstration Plant;
197V
6.
7. AiitHu.-!- '
K, Thomas Neff
K-l
3- Hen urn in- Orjjani/.a:iun Rep
-Nu.
?. fVrrurmn< Urbanization Name anj Acore
A, M. Kinney, Inc.
Consulting Engineers
Cincinnati, Ohio ^5219
10. Protect,'Task, 'Aork Unit No.
G06-EC-0019^
IT. Contract'Gram No.
Final
J 2. Sponsoring Organization Name anJ AJcfress
U.S. Environmental Protection Agency
Office of Solid Waste Management Programs
Washington, B.C. 20U60
13. Type of Re-pore A: Peric.nl
Covered
14.
!5. Si;pp!emencar> Notes
Interim report available from NTIS as PB 213 6k6
16. A
The Franklin, Ohio, resource recovery demonstration project has elicited widespread
interest. This report was prepared to: (l) present a preliminary analysis
of the solid waste disposal and fiber recovery portions of .the project; (2) provide
preliminary data by which others may be guided in evaluating emerging solid waste
disposal and resource recovery technologies. The historical development of this
EPA-sponsored project and a general description and evaluation of the process used
are included. The preliminary plant economics presented are based on construction
costs and the first 12 months of operation. The plant began functioning in June 1971 £
is now in regular operation recovering .ferrous metals and paper fibers which are
to local industries.
nd
17. Kc > Uords r.nJ Document Ana!;, sis. 17a. Descriptors
*Refuse disposal, ^Materials recovery, Incinerators—refuse disposal, Size reduction
(comminution), Wet mills, Magnetic separators, ^Reclamation—salvage, Sludge disposal
"Solid waste disposal, ^Resource recovery, Fluid bed incinerator, Solid waste
separation technology, Liquid cyclone separator, Paper fiber recovery system, Sewage
cluclge disposal, Franklin (Ohio)
13B
Reproduced by
NATIONAL TECHNICAL
INFORMATION SERVICE
US Department of Commerce
Springfield, VA. 22151
Environmental Protect;-- •.- --.
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^SBOlZr- - -
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FRANKLIN, OHIO'S
SOLID WASTE DISPOSAL AND FIBER RECOVERY DEMONSTRATION PLANT
Final Report
VOLUME II
This report (SW-47d.2) was prepared
for the City of Franklin, Ohio, under demonstration grant No. G06-EC-00194
from the Office of Solid Waste Management Programs
by N. THOMAS NEFF and N. WAYNE OKEL
A. M. Kinney3 Inc., Consulting Engineers,Cincinnati, Ohio
A summary report (SW-47d.3) on this project is being published
by the U.S. Government Printing Office
U.S. ENVIRONMENTAL PROTECTION AGENCY
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This report has been reviewed, by the U.S. Environmental
Protection Agency and approved for publication. Approval
does not signify that the contents necessarily reflect
the views and policies of the U.S. Environmental Protection
Agency, nor does mention of commercial products constitute
endorsement or recommendation for use by the U.S. Government.
An environmental protection publication in the solid waste
management series (S
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FOREWORD
The initial objective of this project, started in 1968, was to
demonstrate an innovative solid waste disposal technique utilizing
wet grinding and subsequent incineration. Later the scope of the pro-
ject was expanded to recycle portions of the solid waste stream. The
facility located in Franklin, Ohio, and designed and operated by the
Black Clawson Co., presently includes the capability to separate
reusable paper fibers and ferrous metals for recycling prior to dis-
posing of the remaining solid wastes. Further construction has re-
cently been completed which has added to the plant the capability
to recover color-sorted glass and aluminum. This pilot plant repre-
sents one of the first successful resource recovery facilities in the
country.
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In addition to dispos_ng of all the municipal solid wastes
generated in Franklin, Ohic, the plant also incinerates sludge from a
nearby sewage treatment plant. This project represents a significant
advance in the state of the art of resource recovery and residuals
management. This small system is a completely unique environmental
control complex which has "bean toured "by visitors from many parts of
the world.
This report is based on data collected during the first 12 months
of plant operation, i.e., June 1971 through May 1972. As such, much
of the information and conclusions presented herein are outdated.
Nevertheless, this report, in two volumes, does present much data
which may "be of interest to people in the solid waste management and re-
source recovery fields. Hence the report was prepared for publication.
The plant has continued to run on a regular basis since May 1972,
and a more rigorous and comprehensive evaluation program is now under-
way. The current evaluation is being conducted under a separate
EPA contract with the Systems Technology Corporation (Systech) of
Dayton, Ohio. Their report should be available in early 1975- We
wish to acknowledge the contribution made by David G. Arella, who served
as the government's officer on this project from December 1971 to
August 197!+.
ARSEIT J. DARNAY
Deputy Assistant Administrator
for Solid Waste Management
IV
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INDEX
SECTION
VOLUME I
PAGE
Abstract viil
\
I Summary and Conclusions 1
A. Summary 1
B. Response to Objectives 3
C. Conclusions 4
D. Recommendations 4
II History and Development of Project 6
III Operations Analysis 11
A. General Description of Process 11
B. Description and Evaluation of Process Streams
C. Operating Problems and Process Improvements
IV Economic Analysis 45
A. Construction Costs 45
B. Actual and Projected Operating Costs
VOLUME II
V Unit Operations Analysis 57
A. General Equipment Requirements 57
B. Solid Waste Disposal Plant Equipment 58
C. Fiber Recovery Plant 76
D. General Plant Equipment 82
VI Influent and Effluent Analyses 84
A. Operating Data Summary 85
B. Analytical Data Summary . 134
C. Graphic Representation of Testing Results 152
D. Sampling, Testing and Analytical Procedures 169
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APPENDIX TITLE PAGE
A Bowser-Morner Reports 174
B A. M. Kinney, Inc., Test Reports 235
C The Black Clawson Company Status Reports 266
ILLUSTRATIONS \
- • — '" ' i—in.—,-ii • \
VOLUME I \
Frontispiece Aerial View of Franklin Plant iif
Figure 1. Environmental Control Complex Flow Diagram 12
Figure 2. Plant Layout 13
Figure 3. Receiving Floor 14
Figure 4. Hydrapulper 15
Figure 5. Magnetic Separator and Liquid Cyclone 18
Figure 6. Fluid Bed Reactor 20
Figure 7. Cyclone Rejects and Junk Remover Rejects -,'.* /^. .\xf..... 26
Figure 8. Paper Fiber Being Loaded for Shipmerft .' 29
TABLES
Table 1 Material Balance 22
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ILLUSTRATIONS TITLE PAGE
VOLUME II
Figure 1. Waste Load Variation 155
Figure 2. Rejects to Landfill 156
Figure 3. Reusable Paper Fiber Recovered 157
Figure 4. Proximate Analysis of Reactor Feed 158
Figure 5. pH Various Plant Waters 159
Figure 6. Settleable Solids in Various Plant Waters (By Volume). 160
Figure 6a. Settleable Solids in Various Plant Waters (By Weight). 161
Figure 7. Biochemical Oxygen Demand of Various Plant Waters .... 162
Figure 8. Total Dissolved Solids in Various Plant Waters 163
Figure 9. Total Suspended Solids in Various Plant Waters 164
Figure 10. Total Volatile Solids in Ash Slurry 165
Figure 11. Total Solids in Ash Slurry 166
Figure 12. Junk Remover Rejects Non-Magnetic Fraction 167
Figure 13. Cyclone Rejects Analysis -68
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Title: System for t.otai ri'/uoe •,', Feb. 28, 1973
Prelect Objectives; To design, construct, operate, and evaluate a demonstra-
tion plant for disposal of municipal solid waste and for the recovery of metals,
glass, and paper fibers therefrom,
The system was designed to receive virtually unsorted municipal solid waste
and to separate it by using a fluid-mechanical process. Reusable paper fibers,
raetals, and noncombustibles are separated in the process, and the remaining com-
b^ystible solids are mixed with sewage sludge from an adjoining sewage treatment
pjant, and then burned in a fluid bed incinerator.
Results of Project: The plant is in daily commercial operation as the
principal solid waste disposal facility for the City of Franklin and adjacent
areas. The technical capability of the Wet Processing and Disposal system has
been successfully Jemonstratic, TLe rl.oer Recovery oystan initially produced
yields cf paper fi^er lower than anticipated, but r.as undergone further develop-
mental work to increase yield.
Actual operating coses during die :;:.c.;> covereo by this report are higher
than originally anticipated d^e to low ^..-a,?*1 (40 cons per day) and due to
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ir.flation. However, sufficient data and operating experience have been obtained
to permit cost projections for plants of larger capacities, which indicate lower
operating costs.
Summaries, tables and graphs are included to present actual construction
and operating costs, as well as influent and effluent operational data.
This report was submitted in fulfillment of Project No. G06-EC-00194 under
the partial sponsorship of the Office of Solid Waste Management Programs,
Environaental Protection Agency.
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SECTION V - UNIT OPERATIONS ANALYSIS
The following specifications and data sheets outline the process equipment
installed in the Hydrasposal system (Solid Waste Disposal Plant) and the Fibre-
claim (Fiber Recovery Plant). Where process changes have been made during the
demonstration period, these specifications and data sheets have been updated,
insofar as possible, to reflect as-built conditions. The specifications have
been excerpted from A. M. Kinney, Inc., Specification No. 01890-01, used to
obtain bids for the process equipment and which formed the basis for the con-
tract under which the process equipment was furnished.
Specifications for certain items of nonprocess equipment furnished by the
construction Contractors are included In the appropriate groupings.
Where MCD is mentioned it refers to Miami Conservancy District.
A. GENERAL EQUIPMENT REQUIREMENTS
1. Electrical Work
a. Motors. Motors 1/2 horsepower and larger, are 230/460 volt, 3-phase,
60 Hz, dripproof, squirrel cage induction type, with Class A or Class B insu-
lation, except that agitator drive motors are totally enclosed and weather
protected (fan cooled or nonventilated). Motors 1/3 horsepower and smaller,
are 115 volt, single phase, split phase, or capacitor start induction type
synchronous speed not in excess of 1,800 rpm.
All motors are designed for across-the-line starting with low starting
current. Motors rated 100 horsepower and larger are equipped with thermal pro-
tection against dangerous overheating due to overload, and stalled rotor, with
integral or separate device having contact capacity to operate directly in
holding coll circuit of motor starter. All motors are provided with terminal
housing of metal and of substantial construction, sized and provided for conduit
entrance indicated.
Motor for each item of equipment is of the make customarily furnished for
the Intended service by the equipment manufacturer, with grease-lubricated ball
bearings of a type suitable for periodic renewal of lubricant.
Motors conform to latest standards of ANSI* IEEE, and NEMA for design,
ratings, performance characteristics, service factor, and tests. Each motor
will carry continuously the maximum possible load developed by the driver's
machine without exceeding the temperature rise specified by NEMA for the insu-
lation classification, and have a najaeplate power rating not less than the
brake horsepower requirement of the driven load under any design condition.
Except for the feed conveyor equipment No. 120, motor starters were furnished
under other specifications.
57
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k- Controls. Electrical control devices are suitable for use on 120 volt,
single phase, ac circuits.
B. SOLID WASTE DISPOSAL PLANT EQUIPMENT
1 Scop--
This section of the specification called for delivery, fob jobsite, of all
equipment and materials and all work necessary for the design, manufacture and
delivery of equipment, motors and accessories. The work included:
Hydrapulper, with lubrication pump
Junk remover
Hydrapulper dump pump
Hydrapulper feed conveyor
Liquid cyclone
Surge chest agitator
Surge chest pump
Thickener
High density press
Press screw feed conveyor
White water chest agitator
White water chest pump
Sludge storage chest agitator
Sludge storage chest pump
Scrubber discharge pump
Sewage sump pump
Fluid bed reactor
Reactor pneumatic conveyor
Fluidlzing air blower
Venturi gas scrubber lining and insulation
Gas cooler
Ash pump
Reactor preheat oil burners and blower
Fuel bed oil injection nozzles
Reactor fuel oil pumps
Interconnecting breeching and stack
Controls and instruments including prewired and piped solid waste
and reactor control panels
Refractory lining in reactor and breeching, including installation
Motors and drives
Supervision of field erection, initial operation, and testing of
equipment furnished hereunder
Furnish, field erect and paint, surge, white water and sludge chests
Scrap metal magnet separator
58
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2. Work Under Other Contracts
Separate contracts were awarded by the Owner for the following related
work:
Erection of all equipment herein specified except: refractory and
corrosion-resistant linings In reactor, breeching and scrubber and
the surge, white water and sludge chests
Equipment and chests foundations
Interconnecting piping
Fuel oil supply tank
Purchase of flowmeters for sewage sludge, white water and process
water
Air compressors
Jib crane
Truck scales
Conveyor and truck scale pit sump pumps
Propane gas bottles with regulator
Antifreeze compressed air distributors in outside tanks
Electrical wiring external to control panel
Interlocks on equipment supplying material to the reactor pneumatic
conveyor
3. Special Requirements
Design and fabrication of structural steel conforms to the latest specifi-
cations of the American Institute of Steel Construction and the Code of Standard
Practice.
Combustion equipment including burners and controls conform to FIA standards,
Design conforms with all applicable laws, codes and ordinances of the City
of Franklin, State of Ohio and Federal Air Pollution Control laws.
4. Capacity and Performance Requirements
System is designed to process (by a. wet process) municipal solid waste at
the rate of 150 tons (as-received basis) per 24 hours, and sewage sludge at the
rate of 7.5 tons (dry solids basis) per 24 hours. Inorganic materials such as
tin cans and glass bottles are separated, and the residual organic material,
containing approximately 85 percent volatiles, burned in a fluid bed reactor.
Solids content of cake at outlet of high density press: 40 percent,
minimum.
Reactor designed for 40 percent excess air.
Burn pulped refuse and sewage sludge at the rate of 132 pounds per minute
(dry basis) without auxiliary fuel except during startup.
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Analysis of pumped refuse and sewage sludge:
Solids content 40 percent
Volatile solids 35 percent
Heat content 8,800 Btu per pound of volatile solids
Combustion rate 425 pounds of dry solids per day per square foot of free-
board area.
Stack gases at scrubber outlet free from odors.
Paniculate matter does not exceed 0.1 grain per standard cubic foot
corrected to 12 percent carbon dioxide.
5. Weighing and Receiving
a. Truck Scale.
(1) General. One truck scale, Toledo Model 2781 MG, furnished and
installed by General Construction Contractor.
Scale is of the concrete platform type with parallel link suspension
members, designed for a maximum capacity of 52 tons with a scale platform 10
feet wide by 45 feet long, in accordance with Handbook 44, Federal Specifica-
tions and Regulations on Scales.
Scale package included lever system, scale head, and all weighbridge
structural steel, pit coping angles, bumpers, foundation bolts and manhole
cover plate.
(2) Accessories. Accessories included the following:
Autorange - automatic control of unit weights
Model 410 Printweigh prints weight simultaneously on inserted
tickets and on a roll strip contained with the Printweigh
housing
Printweigh housing is key locked
Manual set date mechanism
Informaplate, permitting up to 44 characters or spaces for
identification
Scale equipped with two head heaters, each 60 watts, 120 volts
ac
Unit is provided with necessary extension levers for
installation as indicated
Manufacturer's mechanics supervised installation and calibration
of the scale
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b. Front End Loader.
(1) General. The front end loader was originally specified for the
project as follows:
Gasoline-fueled, internal combustion engine-driven, four wheel drive,
rubber pneumatic-tired compact type front-end loader, similar and equal to
Bobcat M-600 unit as manufactured by Melroe Division of Clark Equipment Company,
with load rating capacity of at least 1,000 pounds and equipped with an approxi-
mately 13 cubic foot utility bucket fitted with an hydraulically operated
grapple having a minimum of five hardened steel tines. This unit was purchased
separately by the City.
Initial operation of the plant showed that this unit did not have
sufficient capacity to keep the feed conveyor fully charged and was subject to
excessive fire wear. The Portman Equipment Company, suppliers of the unit,
offered to refund the full purchase price of the Model M-600 in exchange for a
Model 970, equipped with a 1-1/8 cubic yard utility bucket and powered by an
85 hp diesel engine. The additional cost of this replacement was $10,950; how-
ever, it was of a design and capacity also suitable for use by the City as a
replacement for the bulldozer previously used in the landfill operation.
c. Feed Conveyor, Equipment No. 120.
(1) General. Unit manufactured by Webster Manufacturing Company was
furnished as part of the process equipment package.
Purpose. Feed refuse from a storage area to the Hydrapulper.
Capacity and Size. Seven tons per hour plus 25 percent surge, pan
width, 60 inches.
Type and -Arrangement. Apron type, arranged for installation in the
apace provided, and to suit the low clearance over the Hydrapulper.
(2) Frame, Hopper, Skirts and Chute. Structural steel supports from
floor without connections to building or equipment. Loading hopper directs
material to horizontal section of conveyor. Skirts are provided on one side
of loading hopper and both sides of inclined section of conveyor. Discharge
chute directs material -into Hydrapulper.
(3) Conveyor. Pans, 60 laches wide, 3/8 inch thick, 4 inch high ends,
steel wearing shoe, pusher bar of structural angles every fourth pan.
(4) Chain. Steel bar buah&d roller chain, high carbon side bars,
carbon steel case hardened bushings., single flanged high carbon heat-treated
pins and through-rods every other link. Pins and through-rods drilled and
supplied with lubrication fittings. Shop-assembled in lengths convenient for
handling.
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(5) Sprockets. Head sprockets, flame-hardened teeth, bored with key-
seat and setscrew.
(6) Bearings. Head shaft, heavy-duty, roller pillow blocks. Foot
shaft, normal-duty screw type take-up with 12 inch travel.
(7) Speed Reducer, Helical and/or herringbone Type AGMA rated; service
factor 1.5 based on motor horsepower. Provided with motor mounting base and
flexible high-speed motor coupling.
(8) Chain Drive. Roller chain, Rex 160. Sprockets, steel cut teeth,
keyseated bore and setscrew. Drive sprocket, flame-hardened teeth and shear
pin hub.
(9) Drive. Variable-speed drive, by impulse from Foxboro M-N2. Con-
sistency Indicator specified hereinafter. Control modulates speed to 50 percent
of conveyor capacity. Control deenergizes unit at below 50 percent capacity.
Motor, 10 horsepower.
d. Conveyor Pit Sump Pump» Equipment No. 136. Weil No. F-800, sump pump,
capacity 15 gpm at 15 foot tdh with I/A horsepower, 1,150 rpm general service
motor.
Pump complete with couplings, Alemite grease fitting, grease lubricated
bronze guide bearings, grease sealed adjustable ball thrust bearing, self-
lubricating lead-bronze bottom bearings, bronze impeller and cast iron suction
strainer.
«. Cash Register. The cash register was purchased separately by the City
from the National Cash Register Company. It was specified to have an indication
window to show both on the front and back of the register the weight in pounds
and money in U.S. dollars and cents recorded. Cash register now has seven
amount rows ($99,999.99) on display window, with accumulating capacity of eight
digits ($999,999.99).
Cash register is an adding type, itemizing register for the purpose of
adding sales and bringing forward new balances on credit accounts, and has the
following accessories and abilities:
Cash register will accumulate the following information in the form
of totals under locked control by the operating company management:
Total number of pounds recorded for any given day
(Matches scale recording)
Total amount of business recorded for any given day
(Cash and credit customers combined)
Total amount of business recorded for cash customers
only, for any given day
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Total amount of business recorded for credit customers only,
for any given day
Total amount of monies recorded from payments on account
Total business (cash, credit and payments on account) recorded
by "A" Weigh-master
Total business (cash, credit and payments on account) recorded
by "B" Weigh-master
Total amount of previous balance pickups recorded for any
given day
Two drawers which operate upon the depression of "A" and "B" Weigh-
master keys, respectively, have removable till trays
Two separate slip insertion tables for use with the scale sales slip
and the customer credit statement/ledger, respectively
Ability to print a consecutive number of each transaction sequence
on the following media:
Scale sales slip
Customer credit statement/ledger
Detail sales journal
An autographic detail sales journal to print all the details of each
transaction in the order in which it occurred. This detail sales
journal is under locked control by the operating company management
Prints the following information on the detail sales journals
Total number of pounds recorded on that transaction
Total amount of money recorded on that transaction
Date of transaction
Consecutive number of transaction
Previous balance owed before transaction
New balance owed after transaction
Monies received as payment on account (if entered on keyboard)
Ability to be subtotaled at any time during the day for the purpose of
knowing any or all of the accumulated information up to that point
of time. This feature is under locked control by the operating
company management
Ability of being totaled out (cleared to zero) at the end of each day
This feature is under locked control by the operating company
management
A nonresettable special counter for the purpose of counting the number
of times the register has been totaled out (cleared to zero)
The following special counters for the purpose of counting the number
of transactions that occurred in any given day:
Cash customer transaction counter
Credit customer transaction counter
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Prints the following information on the scale sales slip:
Total amount of money recorded on that transaction
Date of transaction
Consecutive number of that transaction
Prints the following information on the customer credit statement/
ledger:
Total number of pounds recorded on that transaction
Total amount of money recorded on that transaction
Date of transaction
Consecutive number of that transaction
Previous balance owed before transaction
New balance owed after transaction
Monies received as payment on account
Ability to create a customer credit statement/ledger with up-to-date
balance suitable for mailing
Payment on account transaction counter
"A" Weigh-master transaction counter
"B" Weigh-master transaction counter
Constructed in such a manner as to allow for the future addition of
some print rows of keys to the left of the keyboard without impairing the accum-
ulating capacity of the register.
The manufacturer of the cash register has cooperated with the City in
preparation and supply of business forms compatible with both cash register and
the scale, and supplied a desk-top pocket file case for retention and filing
alphabetically the customer credit statement/ledger cards.
f. Desk Calculator. Electronic calculator, with no memory, capable of
adding, subtracting, multiplying and dividing, and has an eye-ease 12 digit dis-
play with overflow and credit balance/minus signal. It has an automatic decimal
point and a constant key, and was purchased by the City from the National Cash
Register Company.
6. Hydrapulper, Equipment No. 101, and
Lubrication Pump, Equipment No. 105
Hydrapulper of adequate capacity to process 13,400 pounds of municipal
refuse per hour, reducing all organic material to pass through 3/4 inch diam-
eter holes.
Drives. Hydrapulper, 300 horsepower, 1,200 rpm. Oil pump, 1 horsepower.
(Note: Equipment No. 102 - Chopper, deleted from Scope).
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7. Hydrapulper Dump Pump, Equipment No. 104
Purpose. Remove slurry from Hydrapulper, circulate it through the liquid
cyclone and discharge either to the solid waste or fiber recovery surge
tanks
Capacity. 500 gpm at 60 foot tdh
Type and Size. Black Clawson 5 inch BN
Features. Impeller and case CA-I5 stainless steel, heat-treated. Roller
bearings, end suction - split case. Adapter on suction connects to
standard pipe size
Motor. 30 hp, 1,200 rpm
8. Junk Remover, Equipment No. 103 and Washer 148A
Purpose. Operate in conjunction with the Hydrapulper to remove and wash
nonpulpable material
Capacity. 3,000 pounds per hour, 60 cubic feet per hour
Type. Junk remover: Chain-operated buckets designed especially for this
service. Washer: Rotating continuous type Ransohoff scrap washer
Features. Provided with water sprays for washing slurry from material
being removed
Junk remover drive. 5 hp motor, 1,800 rpm conveyor speed, 40 fpm.
Washer drive. 1/2 hp with sycrogear chain, barrel speed 5 rpm
9. Scrap Metal Magnetic Separator,
Equipment No. 148B and 148C
General. Furnish and install magnetic separator, chutes and supports be-
tween junk remover outlet and skip hoist.
Function. Receives total output of junk remover item No. 103, magnetically
separates ferrous scrap metal, discharges ferrous scrap to first 60 inch deep
drop-bottom hopper, and discharges nonmagnetic scrap to a second 60 inch deep
drop-bottom hopper.
Features. Constructed of materials suitable for wet junk operation and
includes furnishing and installing of all separator components, conveyors and
conveyor supports, inlet chutes and outlet separator curtains.
Transport conveyor from washer discharge to magnetic separator is a 24 inch
rubber belted conveyor with cross-flights on approximately 24 inch centers,
200 fpm speed and is powered by a 3/4 hp motor.
Electromagnet has 300 fpm face conveyor, rubber belted with aluminum cross-
flights, and is powered by a 2 hp motor.
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10. Liquid Cyclone. Equipment No. 106
Purpose. Remove heavy and coarse particles from the slurry discharged
from the Hydrapulper
Capacity. 500 gpra with a pressure drop of 20 psi
Type and Size. Black Clawsoi1.., assembly No. 10
Features. Self-contained. Wearing sections, ceramic linede Rejects
chamber with inlet and outlet valves which are air-operated and auto-
matically controlled by timer
11. Liquid Cyclone Rejects Conveyor, Equipment No. 121
Purpose. Convey rejected solids from liquid cyclone discharge to drop-
bottom hopper
Type and Size. Link-belt screw, 12 inches in diameter and 8 feet 10 inches
long
Features. Trough, 430 stainless steel, perforated one-third the length
with holes 1/16 inch diameter. Screw, carbon steel
Drive. 5 hp motor
12. Surge Chest, Equipment No. 127
Purpose. Receive slurry from the liquid cyclone and rejects from fiber
recovery plant
Capacity. 60,000 gallons
Chest fabricator supplied steel channel base ring, which was set in con-
crete foundations under other specifications. Sides were then field-welded to
base ring. After chest was completed, concrete sloping cone bottom was installed
in chests by General Construction Contractor.
Structural steel shapes. A 36
Plate. Commercial quality hot rolled steel
Welding was in accordance with American Welding Society standards. Chest,
complete with connections, was sandblasted and painted with two coats of epoxy
paint after erection.
Chests and tanks equipped with Walker Process, Spargers complete with U-
bolts, diffusers and mounting plate gaskets, through which compressed air is
blown to prevent tanks and chests from freezing.
13. Surge Chest Agitator. Equipment No. 107
Type. Black Clawson cone, for metal chests
Material. Cast iron construction
Drive. 75 hp, 900 rpm motor, V-belt, with cover for outdoor service
Purpose. Maintain uniform consistency in surge chest
Features. Propeller coated with Ceilcote
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14. Surge Chest Pump, Equipment No. 108
Purpose. Remove slurry from surge chest and deliver It to the thickener
Capacity. 500 gpm at 60 foot head
Type and Size. Black Clawson 5 inch BN
Features. Impeller and case CA-15 stainless steel. Roller bearings -
end suction - split case. Adapter on suction connects to standard pipe
size
Motor. 25 hp, 1,200 rpm
15. Thickener, Equipment No. 109
Purpose. Remove water from slurry and thereby increase concentration of
solids from 3.5 to 10 percent
Capacity. 350 gpm
Type and Size. Black Clawson, 3-barrel with three 16 inch inclined screws
Material. Mild steel housing and screw, stainless steel basket
Drive. Each screw by individual 15 hp motor with V-belt drive
16. Screw Conveyor. Equipment No. lllb
Purpose. Convey material from the thickener to the press
Capacity. 50 tons per hour (material as received)
Type and Size. Screw conveyor, 12 inch diameter
Material. Mild steel screw and trough
Drive. 3 hp motor
17. High Density Press. Equipment No. 110
Purpose. Remove water from slurry discharged from the thickener and from
the sewage treatment plant sludge and thereby increase the concentration
of solids to 40 percent
Capacity. 95 tons (oven-dry solids) per 24 hour day, 132 pounds per
minute
Type and Size. Rietz Manufacturing Company, "V" Press Model RVP 60
Features. Press wheel diameter 5 feet. Provided with locally mounted
control panel with local hand-off-automatic switches for each motor.
Local panel includes all necessary transducers, timing and limiting
devices, Interlocks and all other control appurtenances not included
in central solid waste plant panel
Drive. One 50 and two 10 hp motors
*
18. Sewage Sump Pump, Equipment No. 147
Purpose. Return water from Hi-Density press and excess white water to MCD
Capacity. 150 gpm at 30 fooc Head
Type and Size. Black Clawson 4 inch, Class JU
Features. Vertical, cast iron bronze-fitted, open impeller, top thrust
bearing, bottom bearing graphite, water lubricated by fresh water feed
through pipe column. Shaft chrome plated
Motor. 7,5 hp
67
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19. Screw Conveyor, Equipment No. Ilia
Purpose. Convey material from the press to the pneumatic feeder
Capacity. 50 tons per hour (material as received)
Type and Size. Screw conveyor, 12 inch diameter
Material. Mild steel screw and trough
Drive. 3 hp motor
20. White Water Chest. Equipment No. 128
Purpose. Receive white water from process and provide a supply for
recycle back into the system
Capacity. 30,000 gallons
Construction. Same as Surge Chest, Equipment No. 127
21. White Water Chest Agitator. Equipment No. 112
Purpose. Maintain uniform consistency in white water closet
Drive, 20 hp, 1,200 rpm motor
General Type. Same as Surge Chest Agitator, Equipment No. 107
22. White Water Chest Pump, Equipment No. 113
Purpose. Remove slurry from white water chest and recycle to the
Hydrapulper
Capacity. 300 gpm at 47 foot tdh
Type and Size. Black Clawson 4 inch BN
Features. Impeller, cast iron construction. Roller bearings - end
suction - split case
Motor. 20 hp, 1,200 rpm
23. Solid Waste Sump Pump, Equipment No. 122
Purpose. Return white water from sump to white water closet
Capacity. 500 gpm at 30 foot head
Type and Size. Black Clawson 4 inch, Class JU
Features. Vertical, cast iron bronze fitted, open Impeller, top thrust
bearing, bottom bearing graphite, water lubricated by fresh water feed
through pipe column. Shaft chrome plated
Motor. 15 hp, 1,200 rpm
24. Sludge Cheat, Equipment No. 129
Purpose. Receive sewage treatment plant sludge and provide a uniform
feed to the Hi-Density press when the plant is operating
Capacity. 46,000 gallons
Construction. Same as Surge Chest, Equipment No. 127
68
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This chest was modified by Black Clawson to approximately half Its design
capacity by Installing a process water clarifier In the upper portion of the
tank. The clarifier Is an air-flotation type of Black Clawson'• own design and
manufacture, and functions to reduce the concentration of liplds and fines In
the white water recirculation system.
25. Sludge Storage Chest Agitator, Equipment No. 114
General-Type. Same as Surge Chest Agitator, Equipment No. 107
Purpose. Maintain uniform consistency in sludge storage chest
Drive. 20 hp, 1,200 rpm motor
26. Sludge Storage Chest Pump, Equipment No. 115
Purpose. Transfer sewage treatment plant sludge from sludge chest to inlet
of Hi-Density press
Capacity. 25 gpm at 30 foot head
Type and Size. Moyno 2-SWG8
Features. Rotor, high-carbon, high chrome tool steel with hard chrome
plating. Stator, Buna-N synthetic rubber. Bearings, radial and thrust,
grease-lubricated.
Drive. Mechanical variable speed drive. Motor, 5 hp
27. Reactor. Equipment No. 130
a. General. The fluid bed reactor was furnished by Dorr-Oliver, Inc., as
a subcontractor to Black Clawson, complete with feed system combustion gas
scrubbers, pumps, burners and blowers. The reactor manufacturer furnished and
installed the refractory and corrosion-resistant linings in the reactor and
breeching on the jobsite.
b. Type and Arrangement. Reactor Includes carbon steel casing which was
prefabricated and shipped to jobsite in sections for field erection complete
with nozzles, manholes, air inlets and gas outlets, insulation and refractory
linings, oil pumps and burners for fuel bed and reactor preheating with pilot
assemblies, manual valves, regulators, transformers, FIA-approved controls and
safeguards, constriction plates, alloy steel tuyeres, access ladders, platforms,
and high silica sand fluid bed "fill." Field erection of the reactor was part
of the mechanical construction work.
c. Capacity and Performance. Burning rate. 132 pounds per minute of a
mixture of fibrous waste consisting of municipal refuse and sewage sludge.
Solids content 40 percent
Volatile solids 35 percent
Heat content 8,800 Btu per pound, volatile solids
69
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This material is burned without the use of auxiliary fuel except for
start-up.
Excess air 40 percent
Bed temperature 1,500 F
d. Materials.
Steel:
Plates A 283, Grade G
Structural members A 36
Welding electrodes A 233, E-60 series
Flanges ANSI B16.5 (plate ring flanges A 283)
Bolts A 307
Stainless Steel:
Sheet and plate A 167, Type 316L and/or 310
High temperature piping Type 316L
Gas ducts Type 304L stainless steel
Refractory:
Rated in accordance with C 24-56 "Standard Method of Test for
Pyrometer Cone Equivalent of Refractory Material"
Castable refractories C 401-60
Fire clay and high alumina refractory brick C 27-60
Insulating fire brick C 155-57
e. Reactor Accessories.
Access doors Into the windbox and the bed area
Preheat burner mount
Reactor feed nozzles
Sand loading and removal system
Fuel oil guns
Platforms
Sight glasses to observe freeboard and fuel ports
Thermocouple and pressure taps
f. Insulation and Refractory Lining.
Insulation of the reactor is sufficient to provide an average skin tempera-
ture of 180F during operation. When the reactor is shut down, the average
temperatures of the inert bed do not decrease at a rate greater than 10 F per
hour while cooling from 1,500 F to 1,200 F.
70
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g. Fuel Oil System. Equipment No. 0331. 0320.
Purpose. Heat bed to a temperature sufficient to permit introduction of the
mixture of pulped refuse and sewage treatment plant sludge.
Capacity. Two preheat burners, 6,000,000 Btu per hour each, burning No. 2
fuel oil. Auxiliary fuel oil is fed into reactor through 18 fuel guns inserted
Into the fluid bed and automatically controlled with three propertionators, with
six guns supplied by each proportionator.
Features. Preheat burner system includes all accessories for coordinated
operation of the reactor system including all necessary valves, pumps, strainers,
gages, switches and interlocks.
Ignition of the main burner is by propane pilot system, including all
necessary controls, valves, igniters and regulators.
Guns are stainless steel, air-cooled and removable.
Pump Drives. One preheat burner pump driven by 1/2 hp motor. One bed
burner pump driven by 1 hp motor.
Eighteen spare bed gun ports installed for future addition of liquid indus-
trial waste guns.
h. Gas Ducts.
Purpose. Provide interconnecting ducts for the flow of gases
Components. Ductwork, hangers and supports, expansion joints, refractory
and thermal insulation
Material. Reactor gas discharge duct, carbon steel, refractory-lined
Stack. Scrubber outlet self-supporting fiber glass reinforced polyester
Features. Ducts, welded construction, flanged and in sections to facilitate
field handling and assembly and maintenance
Water sealed expansion joint in vertical sections to maintain alignment be-
tween equipment and prevent excessive stresses from being transmitted to
equipment as a result of temperature variations
Supports to prevent vibration, sagging or excessive stresses, with adequate
drawings to instruct Installation Contractor
i. Electrical Interlocks.
(1) Preheat Burner. All necessary interlocks provided for the follow-
ing system conditions in the reactor control panel.
Any of the following conditions automatically shuts off all fuel to
and extinguishes the preheat burner flame:
71
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Preheat burner blower stopped
Preheat burner combustion airflow below a preaet rat*
Any momentary or extended power failure
Flame failure (once flame Is established)
(2) Bed Guns. Any of the following conditions automatically shuts off
the fuel to the bed fuel guns:
Bed temperature below 1,150 F
Bed temperature above 1,600 F
Fluidizing airflow below a preset rate
Any momentary or extended power failure
High gas temperature to scrubber
(3) Pneumatic Conveyor. Any of the following conditions automatically
shuts down the pneumatic feed conveyor to the reactor:
Bed temperature below 1,200 F
Bed temperature above 1,600 F
Pluldizing airflow below a preset rate
Any momentary or extended power failure
High gas temperature to scrubber
Interlocking connections are provided for stopping equipment supply-
ing the pneumatic feed conveyor.
28i. Preheat Burner Blower, Equipment No. 1*2
Purpose. Atomize the fuel oil and supply the preheat burner combustion
air
Capacity. Rated A,500 scfm at 2.0 psig
Type. Centrifugal, multistage design incorporating rotor, housing and
antifriction bearings
Features. Complete unit mounted on common base, including flexible cou-
pling, motor, coupling guard, vibration absorbing pads, companion
flanges, rubber sleeves and clamps. Bearings, antifriction, grease
lubricated
Drive. 60 hp motor
29. Scrubber. Equipment No. 13la and
Venturi, Equipment No. 131b
Purpose. Remove particulate matter from the products of combustion dis-
charged from the reactor
Capacity. Cool 71,800 cfm of combustion gases from 1,570 F to 182 F by
introduction of 81.5 gpm of water
Ash removed by discharging 30 gpm of water from the scrubber system
72
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Material. Corrosion resistant construction. Venturl scrubber throat
elbov and scrubber separator section lined with acid brick. Cooling
section constructed of carbon steel lined with polyester
Features. Provisions have been made to permit future application of
additional water introduced into top section of scrubber and trays to
cool stack gases to 120 F
30. Fluidizing Air Blower, Equipment No. 118
Purpose. Furnish fluidizing air to the reactor windbox
Capacity. Rated 14,850 scfm at 4.4 psig, inlet air temperature 70 F
Type. Centrifugal, multistage design incorporating rotor, housing and
antifriction bearings
Features. Complete unit mounted on common base, including flexible
coupling, motor, coupling guard, vibration absorbing, pads, companion
flanges, rubber sleeves and clamps
Bearings. Antifriction, grease lubricated
Drive. 500 hp motor
31. Pneumatic Conveyor With Rotary Feeder. Equipment No. 119
Purpose. Feed the mixture of pulped refuse and sewage-treatment-plant
sludge Into the reactor
Capacity. 132 pounds per minute on a dry basis, with an actual solids
content of 40 percent
Manufacturer. Allen Sherman Hoff
Drives. Pneumatic conveyor, 30 hp motor, rotary feeder, 2 hp motor
32. Scrubber Recycle Pump, Equipment No. 116
Purpose. Circulate water in the Venturi scrubber
Capacity. 600 gpm
Type and Size. Centrifugal Dorr-Oliver, Inc., Model OB-1
Features. Case and cover Hypalon. Impeller Kynar, motor and pump on
common base
Drive. "V" belt, 25 hp motor
33. Ash Discharge Pump, Equipment No. 117
Purpose. Deliver ash from the Venturi scrubber system to the MCD clari-
fier distribution chamber
Capacity. 30 gpm at 20 foot head
Type and Size - Morris - 1 JC8
Features. Cast iron, Ni-hard fitted, especially engineered for handling
abrasive slurries
Drive. Direct-connected motor, 3/4 hp, 900 rpm
73
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34. Fuel Oil Storage Tank and Accessories
a. Tank. Furnished by Mechanical Construction Contractor, on* 5,000
gallon underground fuel oil storage tank, constructed of welded 1/4 inch thick
steel plate, and fitted with 20 inch manhole and bolted gasketed cover, piping
connections and internal piping all sised and located as indicated. Base metal
of tank thoroughly cleaned after fabrication and coated with two 3/32 inch
thick cpats of cold-applied processed coal tar enamel, Kopper's Bitumastic
No. 50, or equal. Tank is Underwriters' Laboratories labeled for storage of
No. 2 fuel oil.
b. Accessories. Preferred Utilities, or equal, accessories as follows:
Fill cap with drain opening, mounted flush with grade
Gage hatch with 3 inch perforated pipe extended to 6 inches from bottom
of tank
Brass screened type vent cap
Single poppet fuel oil foot-valve with 20 mesh monel screen. Set bottom
ol: strainer 6 inches from bottom of tank
35. Heating System Fuel Oil Pumps -
Equipment No. 145A and 145B
Roper Model 34AM005, rotary type fuel oil pump, close coupled with relief
valve, mechanical seals, cast iron housing, bronze bearings and hardened
steel gears and shafts
Capacity. 6.3 gph
Motor. 1/4 hp general service, mounted on common baseplate with pump,
with coupling and coupling guard
36. Fuel Oil Strainer - Equipment No. 144
Andale No. 104B, 2 inch duplex strainer, cast iron, basket type, with
stainless steel 40 mesh wire cloth basket and 125 pound flanged connections.
37. Jib Crane and Hoist, Equipment No. 135
a. General. The General Construction Contractor furnished and installed
one job crane, hoist and trolley, of the following specifications:
Height. 18 feet 1 inch (crane base to bottom of boom)
Length. 15 feet 7 inches (mast center to extreme limit of boom)
Hook Position. 15 feet 0 inch (mast center to extreme hoist hook
position)
Mast. 18 inch diameter
Head Assembly. Maximum dimensions, 5 feet 1 inch (boom to bottom of
head assembly), 1 foot 7 inches (center boom to outside edge of head
assembly)
74
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Rotation. Nominally 360 degrees, except for interference with feed conveyor
cover. Manually rotated on roller bearings
Capacity. 4,000 pound live load, plus weight of hoist
b. Jib Crane. Floor mounted, self-supporting pillar type Jib without
counter weight, Abell-Howe, Type J-904.
c. Hoist and Trolley. Electric hoist, McCollum Hoist & Manufacturing Co.,
low headroom hoist, Type LHE, 4,000 pound capacity, 4 feet per minute speed.
Hoist is complete with required electrical components, Including cord reel
and push button control station mounted on pillar.
38. Forklift Truck
a. General. The City purchased from Moon Equipment Co., on the basis of
Separate bids, one Yale gasoline-powered industrial forklift truck, as specified
herein, for handling containers 56 inches wide by 42 inches long.
The specifications were not intended to limit bidding to any one or to
several manufacturers, and bidders were invited to submit proposals based on
their standard design of equipment to perform the Intended function.
b. Capacity. Load at 24 inch load center through 154 inch maximum fork-
lift, 4,000 pounds.
c. Dimensions.
Maximum fork height 104 inches minimum
Overall height collapsed 87 inches maximum
Free lift 16 inches minimum
Driver overhead guard height 90 inches maximum
Fork length 48 inches
Maximum turning radius 85 inches
d. Performance.
Maximum travel speed 8 mph minimum
Maximum loaded lifting speed 65 fpm minimum
e. Auxiliary Lifting Device. Hydraulic drop-bottom box dumper for handling
and dumping 56 inch wide, 42 inch long and 30 inch deep hoppers manufactured by
The Union Metal Mfg. Co., without alteration to these hoppers. Attachment also
operates with similar 60 inches deep drop-bottom hoppers. Truck and attachment
handles hoppers of either height interchangeably without adjustment.
75
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C. FIBER RSCOVERY PLANT
1. Scope
The work under this division included the following equipment which was
originally furnished by Black Clawson for installation in the Fiber Recovery
Plant by the Mechanical Construction Contractor.
Class!finer
Selectifiers
Centri-CIeanera
Inclined screw thickener
Rietz press (high density)
Side hill thickener
Gyro-flote screen
Class!finer feed pump
Rejects pump
Cleaner supply pump
Side hill white water sump pump
Side hill stock sump pump
White water pump
Selectifier pump
White water chest
Controls and instruments Including prewired and piped control panel
Motors and drives
Supervision of field erection, Initial operation, and testing of
equipment furnished under this division
2. Work Under Other Contracts
Separate contracts were awarded for the following related work:
Erection of all equipment specified herein
Equipment, tank and chest foundations
Interconnecting piping
Electrical wiring external to control panel
Fiber recovery surge tank
Rejects tank
Cleaner supply pump dilution tank
Selectifier dilution tank
Truck loading conveyors
Supports for side hill thickener
Interlocks for sequence starting and stopping of equipment except as
otherwise specified
Furnishing and installing pressure gages
Providing sampling connections
76
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3. Capacity and Performance Requirements
System is designed to accept a slurry of 4 percent solids at the rate of
122 pounds of dry solids per minute, and extract therefrom approximately 50 per-
cent of the paper fiber contained therein. The extracted paper fiber is cleaned,
screened, and dewatered to approximately 40 percent solids, and is in a commer-
cially marketable condition.
4. Classlfiner. Equipment No. 201
Purpose. Receive 1 percent slurry as pumped from the fiber surge tank,
remove foreign material, discharge accepts to selectifier dilution
tank and rejects to the Gyro-flote screen
Capacity. 600 gpm of 3 to 4 percent slurry
Type and Size. Black Clawson, Type V-R
Drive. 150 hp motor
5. Gyro-Flote Screen, Equipment No. 223
Purpose. Receive the rejects from the classifiner and the 12P selectifier,
recycle accepts to the fiber surge tank and discharge the rejects to the
reject tank
Capacity. 600 gpm of 2 percent slurry
Type and Size. Black Clawson's No. 2 Gyro-flote screen.
Features. Complete with screen sprays and accessories except accepts
collection box and rejects chute and trough were provided under other
specifications
Drive. 5 hp, 1,800 rpm motor
Note: This item of equipment proved ineffective and was removed after being
bypassed for most of the demonstration period. It was replaced by the 24P
Selectifier screen initially used as Equipment No. 203.
6. Selectifier 24P, Equipment No. 203
Purpose. Receive 0.6 percent slurry as pumped from the selectifier dilu-
tion tank and discharge the rejects to Equipment No. 204 and accepts
to cleaner supply pump dilution tank
Capacity. 2,500 gpm of 0.7 percent slurry
Type and Size. Black Clawson 24P pressure screen
Features. Screen .062 inch diameter holes
Drive. 25 hp 1,800 rpm motor
Note: This item was replaced by a 36P Selectifier screen as part of Black
Clawson's design changes intended to Increase fiber yield.
77
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7. Saleetifier 12P. Equipment No. 204
Purpose. Receive 0.7 percent slurry rejects from Equipment No. 203 and
discharge rejects to the Gyro-fiote screen and accepts to the selecti-
fier dilution tank
Capacity. 900 gpa of 0*7 percent slurry
Type and Size. Black Clawacn 12? pressure screen
Features. Screen, .062 inch diameter holes
Drive. 10 hp, 1,800 rpm motor
Note; This equipment was replaced by a new 24P Selectifier screen similar
to Equipment No. 203 as part of Black Clawson's yield improvement design change
program.
8. Centri-Cleaners. Equipment No. 207
Purpose. Receive slurry as pumped from the cleaner supply pump dilution
tank, separate and remove small heavy particles and very fine fibers
from slurry, and discharge accepts to hydrasieve units and rejects to
the reject tank. Makes provision for recycle to cleaner supply pump
dilution tank
Capacity. 1,700 gpm
Type and Size. Bauer Bros. Centri-cleaners: 16 units No. 606-110?
9. Hydrasieve Units, Equipment No. 210a, b, and c
Purpose. Receive slurry from centri-cleaners, and separate paper stock
from water. Deposit stock in separate pits beneath the thickener
Capacity. Inlet flow 1,500 gpm
Type and Size. Bauer Brothers, 4.8 inch width
Features. Screen mounted on steel frame support.
Note: This equipment was altered during the demonstration period by the
addition of spray headers in order to increase the effectiveness of the screens.
10. Incline Screw Thickener, Equipment No. 208
Purpose. Receive and reduce water content of stock pumped from the hydra-
sieve units pit. Discharge accepts containing 12 percent solids into
the Rietz press and liquid rejects into the white water tank
Capacity. Inlet flow 175 gpm
Type and Size. Black Clawson 2 barrel with 9 inch inclined screws
Materials. Mild steel housing and screw and stainless steel basket
Drive. Each screw by individual 5 hp motor with V-belts
11. Rietz Press, Equipment No. 209
Purpose. Remove water from stock discharged from the thickener, Increas-
ing the concentration of solids to approximately 40 percent
78
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Capacity. 30 tons (oven-dry solids) per 24 hour day. (42 pounds per
minute.)
Type and Size. Rietz Manufacturing Company, V-press Model RVP 36
Features. Press wheel diameter 3 feet. Locally mounted control panel
with local hand-off-automatic switches for each motor-local control
Interlocks and all other control appurtenances not included in central
fiber recovery plant panel
Drives. One 20 and two 5 hp motors
12. Pumps
a. Classifiner Feed Pump, Equipment No. 202
Purpose. Remove slurry from fiber recovery surge tank, circulate it
through the VR classiflner and discharge into selectifier dilution tank
Capacity. 1,800 gpm at a head of 60 feet
Type and Size. Black Clawson 8 inch, Class BN
Features. Impeller and casing CA-15 stainless steel heat-treated, roller
bearings, end suction, split case, companion flanges on suction and
discharge to convert to standard pipe sizes
Drive. 25 hp 900 rpm motor, V-belts
b. Rejects Pump, Equipment No. 205
Purpose. Return rejects to the solid waste plant surge chest
Capacity. 250 gpm at a head of 40 feet
Type and Size. Black Clawson 5 inch, Class BN
Features. Impeller and casing CA-15 stainless steel heat-treated, roller
bearings, end suction, split case, companion flanges on suction and
discharge to convert to standard pipe sizes
Drive. 15 hp, 1,200 rpm motor, V-belt
c* Cleaner Supply Pump, Equipment No. 206
Purpose. Circulate slurry through the centri-cleaners
Capacity. 1,700 gpm at 120 foot head
Type and Size. Black Clawson 3 inch, Class ANI
Features. Horizontally split, double suction. Nickel cast iron casing,
stainless steel fitted. Open type impeller. Roller bearings. Shaft,
hot rolled alloy steel. Split glands - flexible coupling
Drive. 75 hp, 1,800 rpm motor
d. White Water Sump Pump, Equipment No. 211
Purpose. Remove white water from sump under side hill thickener and
discharge it into the white water chest
Capacity. 1,400 gpm at a head of 30 feet
Type and Size. Black Clawson 8 inch, Class JU
Features. Vertical. Open impeller. Top thrust bearing, cast iron bronze
fitted. Shaft, chrome plated. Bottom bearing, graphite, water lubricated
by fresh water supplied through pipe column
Drive. 25 hp, 900 rpm motor
79
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e. Stock Sump Pump, Equipment No. 21?
Purpose. Remove paper stock from side hill thickener sump and deliver to
inclined screw thickener
Capacity. 165 gpm at 40 foot head
Type and Size. Black Clawson 4 inch, Class JU
Features. Vertical. Open impeller. Top thrust bearing, cast iron bronze
fitted. Shaft, chrome plated. Bottom bearing, graphite, water lubri-
cated by fresh water supplied through pipe column
Drive. 10 hp, 1,200 rpm motor
f. White Water Pump, Equipment No. 213
Purpose. Recycle white water back to the Hydrapulper In the solid waste
plant
Capacity. 1,500 gpm at 30 feet tdh
Type and Size. Black Clawson 8 inch, Class ANI
Features. Horizontally split. Double suction., Cast iron bronze-fitted,
casing. Open type impeller roller bearings. Shaft, hot rolled alloy
steel. Split glands. Flexible coupling with coupling guard
g« Selectifier Feed Pump, Equipment No. 222
Purpose. Receive water from the selectifier dilution tank and circulate
it through the 36P selectifier into the cleaner supply pump dilution
tank
Capacity. 2,300 gpm at a head of 55 feet
Type and Size. Black Clawson 10 inch, Class AN1
Features. Horizontally split, double suction, nickel cast Iron casing.
Open type Impeller roller bearings. Shaft, hot rolled alloy steel,
split glands, flexible coupling and coupling guard
Drive. 40 hp, 1,200 rpm motor
13. White Water Chest. Equipment No. 216
Purpose. Receive white water from the process and supply the pump which
recycles the white water
Capacity. 10,000 gallons
Features. Shop fabricated with sloping bottom and connections as shown
Structural Steel. A 36
Plate. Commercial quality hot rolled steel
Welding. American Welding Society standards
Painting. Sandblasted and two coats of shop applied epoxy paint
14. Tanks
The Mechanical Construction Contractor furnished the following tanks,
each having open tops with 3/8 inch thick steel sides and 1/4 inch thick steel
bottoms. Tank dimensions were as follows:
80
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Equipment Equipment Diameter. Height,
Number Name Feec ,
217 Fiber Recovery Surge T&nk 12 9
218 Rejects Tank 5 7
219 Cleaner Supply 3ilv,ti.;^. ':.c:,k I 10
221 Selectifier Dilution 1V£.k 10 7
Tank height is measured, from t.O;» o>£ ccmcr^'cc. Dotting ring to top of tank.
Tanks were furnished with all aupporii*, t,kirue, gasket u, bolts, nozzles,
piping connections, and sloping concrece vuz poui.ed in bottoms after erection.
Tanks are all-welded carbon sce.~-.-i. eoiistructi.on, having butt welded joints
with complete penetration. Tanks weic cie&ued ar4d puint&d la strict accordance
with Steel Structures Painting Council Specification SSPC-PS4.04-64T., vinyl
paint system No. 4.04. Finish vinyl co&V. color was as selected by the Engineers.
15. Truck Load lag Conveyor No._ 220
The Mechanical Construction Concractor furnished arid installed a Link-
Belt, carbon steel construction, rleiicoid flight acrew conveyor complete with
12 inch diameter screw, flanged ctau,,-,.* wico flush and discharge and inlet
spout, trough ends, cover plairts :.;•;» d e^ecrclc motor drive on Inlet end. The
conveyor is 16 feet 8 inches lon^ ,acs.'.:;ur«d from the centerline of the inlet
spout to the centerliue of the discharge t^out, and la capable of handling 40
pounds per minute of paper pulp eovtiuitxilri& 60 percent moisture, when installed
at an angle of approximately 45 degi^es.
16. Tv.T.
The Mechanical Construr.tion l^o-iLvacuor furnished and installed a Link-
Belt, carbon steel construct ion - Rclicoid flight screw conveyor complete with
12 inch diameter screwB flanged trough with three discharge spouts located as
shown on the drawings, two rack and pinio-c flat aide discharge gates with
extended chain wheel operators as; indicated on the drawings, trough ends,, trough
cover plate with inlet spout, end sl^eiric motor drive „ Conveyor is 13 feet
0 inch long measured from the center. iv c oi the inlet spout to the centerline
of the last discharge spout., ano :,•.» c£ •.«:.,... a of handling 40 pounds per minute
of paper pulp containing 60 pei'c∋ •'i:,iscv. 'e, wnen installed in a horizontal
position,.
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D. GENERAL PLANT EQUIPMENT
The following items of equipment serve all functions and areas of the com-
bined plant.
1. Air Cpm£_rj!9-sar.3_, and _ Accessories
a. Compressors, Equipment No, _ljjA__emd 137B
The Mechanical Construction Contractor furnished and installed two
Worthington Type R, Model 140-30, oil-cooled sliding vane type air compressors,
each rated at 140 scfm at 100 psig discharge pressure with 30 hp general
service motor.
Each unit is a complete factory-wired-and-piped compressed air plant with
all integral components including:
Compressor
Motor and motor starter
Capacity controls
Safety controls
Oil system
Control panel
Cooling air system
Compressed air inlet filter
Silencers
Each unit is housed in a steel factory-painted enclosure, and was furnished
with an across-the-line motor starter, with three leg thermal overload protec-
tion, dual capacity control, combination modulating and timed on-off
Automatic safety controls include high oil temperature switch, high air
temperature switch, high air pressure switch, unloaded start switch, and safety
valve.
Oil system Includes gage, separator, internal filter and air-cooled radia-
tor type oil cooler.
Each compressor package was provided with a pipeline-mounted aftercooler,
single shell type, complete with cyclone separator and automatic moisture trap,
to cool discharge air to within 15 degrees of incoming water temperature.
Control panel mounted on enclosure includes start-stop buttons, indicator
light, discharge air pressure gage, hour meter and demister button.
82
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b* Receiver. 36 inch diameter by 96 inch height vertical air receiver
tank, ASME labeled for 100 psig working pressure, and furnished with gage glass,
drain trap and pressure gage.
c. Oil Filters, Equipment No. 139. System mounted oil filters are Del-
tech Model 150, rated for 140 scfm with a maximum pressure drop of 3.0 psi.
d- Air Dryer, Equipment No. 140.
Wilkerson Air Rite, Model 4308-75, refrigerated air dryer
Capacity, 100 scfm at 100 psig, outlet air dew point 35 F
Unit completely factory piped and wired
83
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SECTION VI - INFLUENT AND EFFLUENT ANALYSES
The following tabulations summarize the physical and chemical data obtained
from plant operating logs, measurements, and analyses of samples taken during
routine monitoring inspections. The sampling and analysis techniques are
described in Subsection C of this section of the report.
Charts of the various streams and their characteristics are included to
graphically present the variations of these characteristics.
84
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A - OPERATING DATA SUMMARY
(48 PAGES)
85
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B - ANALYTICAL DATA SUMMARY
150
Sheet 16
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C. GRAPHIC REPRESENTATION OF TESTING RESULTS
The graphs on the following pages have been prepared from the data com-
piled and tabulated in the foregoing sections.
The only specific trends that can be noted from these graphs are:
1. The waste loads are higher during the summer months than during the
winter months, (See Figure 1) and conversely:
2. The heating value of the organic rejects tends to be higher in the
winter months than during the summer months. One of the reasons for this may be
the increased paper content of the solid waste received during the winter months.
The graphs of the analytical data indicated that while the number of
samples of organic rejects collected during the early stages of the evaluation
period were more than adequate, more frequent sampling of the various plant
waters, cyclone rejects, and junk remover rejects were needed. The sampling
schedule was revised to obtain a more equitable balance between the items
sampled.
The following specific comments are offered:
Figure 1. Waste Load Variation
The extremely high peak experienced during April, 1972, was due
to material received from outside the normal collection area.
Figure 2. Rejects To Landfill
Note that the liquid cyclone rejects make up the largest part of
this stream. Also, the rapid variation of the nonprocessible materials is due
to somewhat erratic handling and recording of the materials and not to variations
in the characteristics of the solid waste received.
152
-------
Figure j. Reusuable Paper Fiber Recovered
The variation shown here reflects the frequent shutdown periods
and partial operation of the fiber recovery system as changes in equipment and
operating procedures were made in an attempt to increase the fiber yield.
Figure 4. Proximate Analysis
Note the variation of the heating value with the seasons, while
the other constituents remain relatively constant. This is deemed to be due to
changes in paper content. With the fiber recovery system operating to its
maximum advantage, this variation would not be so pronounced.
Figure 5. pH of Various Plant Waters
The rise in ash water pH is due to a proprietary chemical added
to the scrubber water to prevent the ash from agglomerating into large lumps.
Figure 6. Settleable Solids
The results of the analyses for this type of solids were at first
reported on a volumetric basis. Since there is no correlation between these
results and the tests for other solids, this test was changed to determine these
solids on a gravimetric basis as shown in Figure 6a.
Figures 7 through 10.
In all the tests on the various plant waters, the widely varying
results reflect the effect of different percentages of water to waste. An opti-
mum blowdown rate was not determined.
153
-------
Figure 11. Total Solids in Ash Slurry
The wide variation shown here is again due to variation in water
flow. The amount of ash discharged was relatively constant. The plant opera-
tors had no reliable means of determining the amount of water being used to
carry this ash to waste.
Figure 12. Junk Remover Rejects Non-Magnetic Fraction
The wide variation in the organic content points up the changes
in washing operations, and the changes in glass content are probably due to
changes in the grinding ability of the Hydrapulper.
Figure 13. Cyclone Rejects Analysis
The variation shown here is due primarily to changes in the
organic content, rather than being due to changes in the glass constituents.
154
-------
Figure 1. Waste Load Variation
155
-------
Figure 2. Rejects to Landfill
156
-------
o » gi -jj JJ g|
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Figure 3. Reusable Paper Fiber Recovered
157
-------
E
Figure 4. Proximate Analysis of Reactor Feed
158
-------
_1TT_LTJ i [__i
Figure 5. pH Various Plant Waters
159
-------
Figure 6. Settleable Solids in Various Plant Waters (By Volume)
160
-------
"t i (aain/ow) sanos aiavaixias -T—rt
Figure 6a. Settleable Solids in Various Plant Waters (By Weight)
161
-------
Figure 7. Biochemical Oxygen Demand of Various Plant Waters
162
-------
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Figure 8. Total Dissolved Solids in Various Plant Waters
163
-------
Figure 9. Total Suspended Solids in Various Plant Waters
164
-------
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Figure 8. Total Dissolved Solids in Various Plant Waters
163
-------
Figure 9. Total Suspended Solids in Various Plant Waters
164
-------
Figure 10. Total Volatile Solids in Ash Slurry
165
-------
Figure 11. Total Solids in Ash Slurrv
166
-------
Figure 12. Junk Remover Rejects Non-Magnetic Fraction
167
-------
Figure 13. Cvclone Rejects Analysis
16ti
-------
H. SAMPLING. TESTING AND ANALYTICAL PROCEDURES
1. General. A representative of A. M. Kinney, Inc., visited the plant
site approximately once a week to obtain operating data and to collect for analysis
samples of the input and output streams.
2. Operating Data. Operating data were tabulated by Black Clawson
personnel on daily log sheets and summarized on weekly log sheets.
These data were then fed to a computer programmed by*A. M. Kinney,
Inc., personnel to:
Tabulate the data
Calculate other information based thereon
Summarize the calculated information for the evaluation period
A print-out of this computerized information is presented in
Heading A of this report.
3. Sampling Procedures. So-called "grab" samples were taken of the
input and output streams when plant operating conditions appeared to be stable.
Samples were taken on different days of the week, and at different times of the
day to minimize the possibility of biased sampling; e.g., when only one type of
refuse was being processed at the plant.
Samples were collected in plastic bags, plastic bottles, or metal
tubs, depending on the stream being sampled; and were of sufficient size to
insure a representative portion of the stream at the time sampled. These samples
were then thoroughly mixed and reduced at the laboratory, using standard sample
reduction methods where applicable to obtain a volume suitable for analysis.
169
-------
The following is a list of the streams sampled; location of the
sample point, and the total number of samples analyzed during the evaluation:
Stream Sample Point No. of Samples
Organic rejects Inlet to pneumatic
to reactor conveyor 68
Junk remover rejects
Magnetic Discharge of magnetic
separator 6
Nonmagnetic Discharge of conveyor
belt 6
Cyclone rejects Discharge of screw
conveyor following
liquid cyclone 9
Waste water Discharge of waste water
sump pump 13
White water Discharge of white water
sump pump 12
Ash slurry Outlet of ash discharge
pump 12
Reactor bed sand Sand discharge nozzle on
reactor 7
Raw refuse input and nonprocessible rejects were not sampled, but
were photographed and a semiqualitative listing of their components was made.
The reactor bed sand analysis was not included in the computer program.
4. Testing Laboratory Analytical Procedures. The samples of organic
rejects, waste water, white water, ash slurry, and reactor bed sand were analyzed
by Bowser-Morner Testing Laboratories, Inc., in Dayton, Ohio, using standard pro-
cedures published by American Society for Testing and Materials (ASTM) American
Public Works Association (APWA) and Scotts' Standard Methods for Waste and Waste
Water, 13th edition, 1971. For reference to specific procedures see the Bowser-
Morner Reports included in Appendix A, Volume II.
A. M. Kinney, Inc., personnel reviewed each laboratory report for
accuracy and for meaningful results, and occasionally requested changes to make
these results more meaningful.
170
-------
The samples of Junk remover rejects were analyzed by A. M. Kinney,
Inc., personnel In A. M. Kinney, Inc., laboratories, using procedures developed
specifically for this evaluation. The details of these procedures are given on
the following pages.
All analytical data were tabulated and summarized by a computer.
A computer print-out of these data are included under Heading B of this section
and are graphically shown on charts presented under Heading A of this section.
5. A. M. Kinney, Inc., Laboratory Testing Procedures.
a. Liquid Cyclone Rejects.
(1) Moisture Determination
(a) Weigh out approximately 300 to 400 grams of wet sample
»
into previously tared pan.
(b) Place in drying oven for approximately 24 hours at
200 F. Stir sample occasionally to insure complete drying.
(c) Calculations.
Weight wet sample and pan
Tare weight of pan
Wet sample weight
Weight dry sample and pan
% Moist - Wt. Wet Sample and Pan - Wt. Dry Sample and Pan x ^QQ
Wet Sample Wt.
(2) Organics.
(a) Use dried sample obtained above. Weigh out approxi-
mately 100 gram sample into porcelain dish. Heat at 750 F (400 C) for two hours.
(3) Size Consist.
(a) Pass remainder of dried sample of (1) above succes-
sively through a No. 4 sieve and No. 10 sieve.
171
-------
(b) Record weight retained on No. 4, that retained on
No. 10,, and that passed by No. 10 sieves.
(c) Calculate percentage that each portion is of the total
sample.,
(4) Physical Composition.
(a) Hand sort material retained on each sieve into the
following fractions:
Clear glass
Green glass
Amber glass
Magnetic metals
Aluminum
Other metals
Large stones
Miscellaneous materials
Weigh each fraction and calculate its percentage of
total sample.
b_. Junk Remover Rejects.
(1) Magnetic Fraction.
(a) Weigh sample.
(b) Hand sort into following categories:
All-steel cans
Steel cans with aluminum tops
Other - identify if possible.
(c) Weigh each fraction and report as a percent of total
magnetic fraction.
(d) Photograph-sorted samples.
172
-------
(2) Nonmagnetic Fraction.
(a) Moisture Determination. Run two samples in conformance
with cyclone rejects procedure. Report average moisture as a percent of the non-
magnetic fraction.
(b) Organic Determination. Use portion of one of dried
samples obtained above and process in conformance with cyclone rejects procedure.
(c) Hand sort remaining dry sample into following fractions
Magnetic metals
Aluminum
Other metals
Glass
Rubber materials
Plastics
Other - identify if possible
Weigh each fraction and calculate its percentage of
nonmagnetic sample.
173
-------
APPENDIX A - BOWSER-MORNER REPORTS
(60 PAGES)
174
-------
£7?
LABORATORY REPORT
August 28, 1972
Report to: A.M. Kinney, Inc. - Consulting Engineers - Laboratory No.
2912 Vernon Place - Cincinnati, Ohio Authorization:
Attn: Mr. Carl Miller
Report on: One Sample of Refuse Submitted for Complete Chemical Analysis
76S20S
The following sample was received from Mr. Wayne Okel by BOWSER-MORNER on July 18,
1972. This sample has the following identification and required analysis:
Bag "BG" for Proximate, Ultimate and Ash Analysis
The analyses were performed in accordance with ASTM Procedure D-271 (Part 19), 1971
F.dition; American Public Works Association for Refuse, Appendix A; and Standard Methods for
Water and Wastewater, 13th Edition, 1971. A discussion of the actual procedures used was
included in our Report No. 759640 (April 14, 1972). The references for the required
analysis are as follows.
Proximate;
Parameter
*r
Moisture
Ash
Volatlles
7ixra-d Carbon
LTU/lb,
Ultimate;
Car'ion
Hydrogen
Nitrogen
Ki.1 cnr
r loorine
Chlorine
Ac 10 Soluble Aluminum
Reference
ASTM-D-271 (Section 8)
ASTM D-271 (Section 11)
ASTM D-271 (Section 14)
ASTM D-271 (Section 17)
ASTM D-271 (Sections 44-47)
APWA, Appendix A, Page 399
APWA, Appendix A, Page 399
ASTM D-271 (Sections 38-40)
ASTM D-271 (Sections 22-23)
Orion Selective Ion Electrode
ASTM D-271 (Sections 3-6)
Perkin-EImer A.A. Handbook
Perkin-Elmer A.A. Handbook
Ash Analysis;
CaO
Wet Chemical Method
Perkln-Elmer A.A. Handbook
Perkin-Elmer A.A. Handbook
Perkin-Elmer A.A. Handbook
Perkin-Elmer A.A. Handbook
(continued)
175
-------
\. M. '"inncy, Inc.
i'a^e 2
U:b. No. 765208
N--.20 Perkin-Elraer A. A.
1<20 Perkin-Elraer A. A. Handbook
Salfite Turbidometric Tltration witb BaCl2
Lead Perkin-Elaer A«A. Har.dbook
ZLSC 'J'c .:."=. 'r,-T 3. -- •-; -.- ':'.' . "'."..
As,. Fusion i-Lish i:'us;;.c", .1^-ab;: .'. . ;~, -•"'.* "~:--
rine sairple was prepared by placing a portion of tbi we.'. -?iavle ;--s, i; beaker ana
drying it at 75°C to determine the moisture content. The dried sample vas then placed
in a "r lender and emulsified as fine as possible. This homogeneous sample was then placed
back in the oven and redried at 75°C. All of the remaining analyses were performed using
the dirked sample. The results of these analyses are as follows.1!
IVoxima t£ . Ar. •i
Moisture, % 53.05
A« ., 7, ' 5,73
Vrtlatiles, % 35.25
Fixed Carboa, % 5.97
BTU/lb. (1st Trial) 7662
BTU/lb. (2nd Trial) 7662
BTU/lb. (Average) 7662
' ! "'..*_ntia t e Anaj-y si s
Carbon, % 45.47
Hydr-.^en, % 6.31
Oxv '. en, % Rem
N: ; rot»cm> % .041
Sulfur, % .33
Chlorine,, % .45
Fluorine, I .001
Na20, % .06
Aci> Soluble Al as ^0, % .71
(continued)
176
-------
A. M. Klnney, Inc.
P, »'• 3
tyib. No. 765208
Ash Analysis Bag "BG"
A1203, % .57 ' -
Si02, % 2,42
Fe20s, % .24
CaO, I .16
MgO, % .26
Na20, % .04
K20, % .17
Zinc, % .024
Lead, % .015
Sulfates, % .003
Ash Fusion
Initial Deformation 2700°F
Softening Temperature 2830°F
Fluid Temperature 2900°F +
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Laboratory
Chem-Met Division
3- Client
2- File
CWK/Jmb
177
-------
LABORATORY REPORT Augu8t 24_ 1972
Report to: A,, M. Kinney, Inc. - Consulting Engine~3 • Laboratory No. 765028
2912 Vernon Place - Cincinnati, Ohio ;"nl& Authorization-
Attn: Mr. Carl Miller
Report on: Five (5) Samples Submitted for Chemical Analysis
Four water samples and one reactor sand sample were received from Mr. Wayne Okel on
August 15, 1972. These samples have the following identifications and required analysis,,
Ash Water (8-15-72) for pH
Total Solids
Volatile Solids
Dissolved Solids
Settleable Solids
White Water (8-15-72) for pH
5 Day BOD
Total Solids
Volatile Solids
Dissolved Solids
Settleable Solids
Waste Water (8-15-72) for pH
5 Day BOD
Total Solids
Dissolved Solids
Seutleable Solids
Clarifier Water (8-15-72) for pH
5 Day BCD
Total Solids
Volatile Solids
Dissolved Solids
Settleable Solids
Reactor Sand (8-15-72) for Sieve Analysis
Silica Content
The above watei samples were analyzed in accordance with procedures outlined in
Standard Methods for Water and Wastewaters, 13th Editiou, 1971. The sieve analysis of the
reactor sand was obtained using procedures in accordance with ASTM (D-11AO), Volume 11,
1970 Edition. The silica content of the reactor sand vus obtained using a wet chemical
filtration method. The results of these analyses are !•<•• follows.
(continued)
178
-------
A. M. Klnney, Inc.
Page 2
Lab. No. 765028
Water Analysis;
I'H
5 Day BOD, mg/1
Total Solids, mg/1
Volatile Solids, mg/1
Dissolved Solids, mg/1
Settleable Solids, mg/1
Reactor Sand:
8H:8
Ash Water
8-15-72
QUA
KiA (iS ij'JM
White Water
8-15-72
9.or
9788
1584
3114
6643
Si02
Sieve Analysis;
12200
9059
5302
3618
4920
Reactor Sand
8-15-72
69.28%
Waste Water
8-15-72
6.23
5250
8346
3810
3802
Clarifier Water
8-15-72
6,84
13700
5235
3700
2352
2653
Sieve Number, US
3/4
1/2
3/8
4
5
6
8
10
16
30
40
50
100
200
Weight Sand
Retained (grams)
0
9
10
53
82
119
206
253
463
849
1084
1272
1298
1299
% Sand Passing
100
99
99
96
94
91
84
81
' 64
35
17
2
0.2
0.1
Sample Weight - 1300 grams
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
JU-KW-
Clyde W. Kayser
Chemist, Instrumentation Laboratory
Chem-Met Division
3- Client
2- File
CWK/jm
179
-------
LABORATORY REPORT
August 16, 1972
Report to: A. M. Kinney Inc. - Consulting Engineers Laboratory No. 764752
2912 Vernon Place - Cincinnati, Ohio 45219 Authorization:
Attn: Mr. Carl Miller
Report on: One (1) Sample of Reactor Fuel Submitted for Chemical Analysis
One (1) sample of reactor fuel was received from Mr. Wayne Okel on August tfr, 1972.
The sample has the following identification and required analysis:
Identification; , Bag "BH" for Proimate Analysis
The analysis was performed in accordance with the procedures outlined in ASTM
D-271, Part 19, 1971 Edition. A discussion of the actral procedures used is Included
in our laboratory report #759640. The references for the proximate analyses are
as follows:
Analytical Parameter Reference
Moisture ASTM D-271 - Section 8
Ash ASTM D-271 - Section 11
Volatile Matter ASTM D-271 - Section 14
Fixed Carbon ASTM D-271 - Section 17
BTU/lb ASTM D-271 - Section 44-47
The sample was prepared by placing a portion of it in a beaker and drying it at
75°C to determine the moisture content. The dried sample was then placed in a beaker
and emulsified as fine as possible. This homogeneous sample was then placed back in the
oven and redried at 75°C. The remaining analyses were performed using this dried sample.
The result of these analyses are as follows:
RECEIVED
AUG171972
(continued) REFERRii TO... —
130
-------
A. M. Kinney Inc. - Consulting Engineers
Page 2
Lab. No. 764752
Proximate Analysis Bag "BH"
Moisture, % 56.28
Ash, % 5.90
Volatiles, % 33.12
Fixed Carbon, % 4.70
BTU/lb (dry) Trial 1 7860
BTU/lb (dry) Trial 2 7874
BTU/lb (dry) Average 7867
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MQRNER Testing Laboratories, Inc.
Clyde W. Kayset
Chemist, Instrumentation Lab.
Chem-Met Division
3 - Client
2 - File
CWK/gmb
181
-------
LABORATORY REPORT
August 8, 1972
Report to: A. M. Kinney, Inc. - Consulting Engineers - Laboratory No. 764432
2912 Vernon Place - Cincinnati, Ohio 45219 Authorization: 604 :
Attn: Mr. Carl Miller
Report on: Three (3) Water Samples Submitted for Analyses
The following water samples were received by BOWSER-MORNER from your firm on July 18,
1972. These samples have the following identification and required analyses.
Ash Water (7-18-72) for pH
Total Solids
Volatile Solids
Dissolved Solids
Settleable Solids
White Water (7-18-72) for pH
5 Day BOD
Total Solids
Dissolved Solids
Settleable Solids
Waste Water (7-18-72) for pH
5 Day BOD
Total Solids
Dissolved Solids
Settleable Solids
i
The above water samples were analyzed in accordance with procedures outlined in
Standard Methods for Water and Wastewaters, 13th Edition, 1971. Using these procedures
the following results are obtained:
Ash Water White Water Waste Water
7-18-72 7-18-72 7-18-72
PH 8.48 5.22 5.25
5 Day BOD, mg/1 - 5650 5700
Total Solids, mg/1 12978 11717 7158
Dissolved Solids, mg/1 2825 4960 4405
Settleable Solids, mg/1 9857 6408 2204
Volatile Solids, mg/1 1481
(continued)
182
-------
A. M. Kinney, Inc.
Page 2
Lab. No. 764432
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
3- Client
2- File
CWK/mj
183
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LABORATORY REPORT
July 10, 1972
Rcpon to: A. M. Kinney, Inc. - Consulting Engineers - Laboratory No. 763133
2912 Vernon Place - Cincinnati, Ohio 45219 Authorization-
Attn: Mr. Carl Miller
Report on: Four (4) Samples Submitted for Analysis
The following three water samples and one reactor sand sample were received by
BOWSER-MORNER from Mr. Wayne Okel on June 2x., 19/2. These samples have the :,Allowing
identification and required analysis:
Ash Water (6-21-72) for pH
Total Solids
Volatile Solids
Dissolved Solids
Settleable Solids
1
Wastewater (6-21-72) for pH
5 Day BOD
' Total Solids
Dissolved Solids
Settleable Solids
White Water (6-21-72) for pH
5 Day BOD
Total Solids
Dissolved Solids
Settleable Solids
Reactor Sand (6-21-72) for Sieve Analysis . , /•*
Silica Content >
The above water samples were analyzed in accordance with procedures outlined in
Standard Methods for Water and Wastewaters, 13th Edition, 1971.
The sieve analysis of the reactor sand was run in accordance with the procedures
outlined in ASTM-D-1140, Part 11, 1970 Edition. The silica content of the sand was
determined by a wet chemical filtration method. Using these procedures the following
results are obtained.
Ash Water Wastewater White Water
Waters: 6-21-72 6-2"-72 6-21-72
pH 10.13 A.70 5.16
5 Day BOD, mg/1 - 6400 9600
Total Solids, mg/1 11435 12082 15514
Dissolved Solids, 1713/1 2002 ' 5552 . 4549
(continued)
184
-------
A. M. Kinney, Inc.
Papc 2
Lab. No. 763133
Ash Water Wastewater
6-21-72 6-21-72
9389 5492
1006
Reactor Sand 6-21-72
78.00%
Weight Sand Retained
By Sieve (grams)
0
39
53
72
119
148
170
273
399
558
788
1040
1068
1074
1077
White Water
6-21-72
10382
—
% Sand Passing Sieve
100
96
95
93
89
86
84
75
63
48
27
4
1.0
.60
.30
Scttlcable Solids, mg/1
Volatile Solids, mg/1
Reactor Sand:
Silica Content
Sieve Analysis:
Sieve Number, US
3/8
4
5
6
8
10
12
16
20
30
40
50
60
70
325
Sample Weight 1080 grams
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
3- Client
2- File
CWK/jm
185
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LABORATORY R iPORT
June 23, 1972
Report to: A. M. Kinney, Inc. - Consulting Engineers - Laboratory No.
2912 Vernon Place - Cincinnati, Ohio 4-3219 Authorization:
Attn: Mr. Carl Miller
Report on: One (1) Sample of Reactor Feed Submitted for Chemical Analysis
762497
The sample was received from Mr. Wayne Okel on June 21, 1972. It has the following «
Identification and required analysis:
Identification: Bag BF for Proximate Analyses
The analysis was performed in accordance with procedures outlined in ASTM D-271,
Part 19, 1971 Edition. A discussion of the actual procedures used is included in our
Report No. 759640. The references for the proximate analysis were as follows:
Analytical Parameter
Moisture
Ash
Volatile Matter
( Fixed Carbon
BTU/lb.
Reference
ASTM D-271
ASTM D-271
ASTM D-271
ASTM D-271
ASTM D-271
(Section 8)
(Section 11)
(Section 14)
(Section 17)
(Sections 44-47)
Temperature
75°C
750°C
950°C
The sample was placed in a beaker and dried at 75 C to determine the moisture conte
The dried sample was then placed in a blender and emulsified as fine as possible. This
homogeneous sample was placed back in the oven and redried at 75°C. The remaining analy
were performed using this dried sample. The results of these analyses are as follows:
Proximate Analysis
Moisture, %
Ash, %
Volatile Matter, %
Fixed Carbon, %
BTU/lb. (Dry) Trial 1
Trial 2
Average
Bag ET
46.27
7.63
40.50
5.60
7555
7461
7508
(continued)
185
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A. M. Kinncy, Inc.
Pngc 2
Lab. No. 762A97
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MDKNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
3- Client
2- File
CLK/jm
187
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LABORATORY REPORT June 8, 1972
Report to: A. M. Kinney, Inc. - Consulting Engineers - Laboratory No. 761871
2912 Vernon Place - Cincinnati, Ohio 45219 Authorization-
Attn: Mr. C. K. Miller
Report on: Four (4) Samples Submitted for Analysis
The following three water samples and one reactor sand sample were received by
BOWSER-MORNER from Mr. Wayne Okel on May 23, 1972. These samples have the following
identification and required analysis:
Ashwater (5-23-72) for pF
Tc olids
Volatile Solids
Dissolved Solids
Settleable Solids
\
Wastewater (5-23-72) for pH
5 Day BOD
Total Solids
Dissolved Solids
f Settleable Solids
Whitewater (5-23-72) for pH
5 Day BOD
Total Solids
Dissolved Solids
Settleable Solids
Reactor Sand (5-23-72) for Sieve Analysis -'- '* ^ '
Silica Content"'
The above water samples were analyzed in accordance with procedures outlined in
Standard Methods for Water and Wastewaters, 13th Edition, 1971. The sieve analysis of tl
reactor sand was obtained using procedures in accordance with ASTM D-1140, Part 11, 1970
Edition. The silica content of the sand was determined using a wet chemical filtration
method. The analyses are as follows:
Waters: Ashwater Wastewater Whitewater
5-23-72 5-23-72 5-23-72
pH 9.81 6.30 5.76
5 Day BOD, mg/1 - 4700 2825
Total Solids, mg/1 28519 25559 13726
Dissolved Solids, mg/1 3718 5597 5957
(continued)
188
-------
A. M. Kinney, Inc.
Consulting Engineers
Page 2
Lab. No. 761871
Waters:
Settleable Solids, mg/1
Volatile Solids, mg/1
Reactor Sand:
Silica Content
Ashwater
5-23-72
14697
2119
Wastewater
5-23-72
19415
White water
5-23-72
7167
Reactor Sand (5-23-72)
77.76
Sieve Analysis:
Sieve Number,US
1/2
3/8
4
5
6
8
10
12
16
20
30
40
50
60
70
80
100
140
200
270
325
Sample Size - 1063 grams
Wt. Sand Retained
By Sieve (grams)
0
2
33
46
64
107
132
156
237
345
505
736
1003
1043
1053
1056
1057
1059
1059
1060
1060
% Sand Passing Sieve
100
100
97
96
94
90
88
85
78
65
52
31
6
2
1
0.7
0.6
0.4
0.4
0.3
0.3
189
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A. M. Kinney, Inc.
Consulting Engineers
Page 3
Lab. No. 761871
Thank you for this opportunity to be of service.
Client - 3
File - 2
CWK/jm
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Irx.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
190
-------
LABORATORY REPORT
June 5, 1972
Report to: A. M. Klnney, Inc. - Consulting Engineers -
2912 Vernon Place - Cincinnati, Ohio 45219
Attn: Mr. Carl Miller
Report on: One (1) Sample of Refuse Submitted for Complete Chemical Analysis
Laboratory No.
Authorization:
761744
604
The following sample was received for analysis from Mr. Wayne Okel on May 9, 1972.
sample has the following identification and required analysis:
Bag J$li for Proximate, Ultimate and Ccr.^..i.ale Ash Analysis
The analyses were performed in accordance with ASTM Procedure D-271 (Part 19), 1971
Edition; American Public Works Association of Refuse, Appendix A; and Standard Methods,
13th Edition, 1971. The analysis ware performed as follows:
Proximate Analysis;
Parameter
Moisture Content
Ash Content
Volatiles Content
Fixed Carbon Content
BTU/lb.
Ultimate Analysis;
Carbon
Hydrogen
Oxygen
Nitrogen
Sulfur
Fluorine
Chlorine
Al2C>3, %, (Acid Soluble
Aluminum)
Ash Analysis;
A1203
CaO
MgO
K20
Zinc
Procedure
ASTM D-271 (Section 8)
ASTM D-271 (Section 11)
ASTM D-271 (Section 14)
ASTM D-271 (Section 17)
ASTM D-271 (Sections 44-47)
Temperature
75°C
750°C
950°C
ppendix A, Jag* 394
,'.PageX399
APWA,
AFJA-,
ASTM D-271 (Section 42)
ASTM D-271 (Sections 38-40)
ASTM D-271 (Sections 22-23)
Orion Selective Ion Electrode
ASTX D-271 (Sections 3-6)
Parkin-Elmer Atonic Al-norption
Perkin-Slmer Atomic Absorption Handbook
Perkin-Einsr Atomic Absorption Handbook
Perkin-Elmer Atomic Absorption Handbook
Perkin-Slner Atonic Absorption Handbook
Parkin-Elmer Atonic Absorption Handbook
Perkin-Zlmer Atoaic Absorption Handbook
(continued)
o
191
-------
A. M. Klnney, Inc.
Page 2
Lab. No. 761744
Lead
Sulfates
Chloride
Trace Metals
Perkin-Elmer Atomic Absorption Handbook
Turbidometric Titration with BaCl2
Mercuric Chloride Titration
Semi-Quantitative Determination by Emission Spectroscopy
An outline of the exact procedures used is included in our Laboratory Report #759640
dated April 14, 1972. The following results are obtained:
Sample Identification;
Proximate Analysis: , ? "
Moisture, %
Ash, %
Volatile Matter, %
Fixed Carbon, %
BTU/lb. (dry sample) (trial 1)
BTU/1b. (dry sample) (Trial 2)
BTU/lb. (dry sample) (Average)
Ultimate Analysis:
Carbon, %
Hydrogen, /£_
Nitrogen, "C
Oxygen, %
Sulfur, %
Chlorine, %
Fluorine,
U
\\-* ' ' '
%
Acid Soluble Al as
Ash Analysis:
A1203, %
Si02, %
Fe203, %
CaO, %
MgO, %
Na20, %
K20, %
Zinc, %
Lead, %
Chlorides, %
Sulfates, %
Bag BE
59.90
4.70
31.08
4.32
7130
7173
7152
18.00
.03
Remainder
.061
.37
.06
.38
.30
1.63
.13
.02
.02
.02
.07
.007
.011
.018
1.49
192
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A. M. KInney, Inc.
Page 3
Lab. No. 761744
Trace Metals: ',
Nickel .0005 - .0025
Titanium , .015 - .050
Copper .0005 - .0025
Tin .0-15 - .0050
Molybdenum 3GI5 - .0050
Lead .0015 - .0050
Manganese - .010 - .050
The values for the proximate and the carbon and hydrogen determinations are on an as
received basis. The remainder of the analyses are calculated to a dry sample basis. The
metal oxides in the ash analysis have been reported as percent of the oxide present in the
original sample. The values for chloride and sulfate have been reported as the percentage
of sulfate or chloride in the ash.
The question has been raised as to whether or not our values for carbon and hydrogen
have been reported on an as received basis or on a dry basis. To check the problem out,
Mr. Fxlward Drinkuth set up the carbon-hydrogen combustion furnace as described in Appendix
A of APWA and obtained the following values.
}V !tf 'I ?>
Sample Identification; Bag AX Bag AW Bag AY
Carbon, % 20.79 19.84 25.94
Hydrogen, % 2.73 2.47 3.47
After comparing these values to our previous values we have come to the conclusion
that these values are on the as received basis. We also feel that our previously reported
values for carbon and hydrogen have also been reported on an as received basis.
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
Client - 3
File - 2
CWK/jm
193
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LAB ORATORY REPORT May 19, 1972
Report to: A. M. Kinney, Inc. - Consulting Engineers - Laboratory No. 75096!
2912 Vernon Place - Cincinnati, Ohio 45219 Authorization:
Attn: Mr. Carl Miller
Report on: Three (3) Samples of Water Submitted for Analysis
The three (3) water samples were received on May 9, 1972 from Mr. Wayne Okel.
These samples have the following identification and required analysis:
Ashwater (5-9-72) for pH
Total Solids
Total Volatile Solids
Total Dissolved Solids
Settlcable Solids
Wastewater (5-9-72) for pH
5 Day BOD
Total Solids
Total Dissolved Solids
Settleable Solids
White Water (5-9-72) for pH
5 Day BOD
Total Solids
Total Dissolved Solids
Settleable Solids
The above water samples were analyzed in accordance with th-p ^proc^dures outlined ii
Standard Methods for Water and Wastewater, 13th Edition, 1971. D^ing these procedures
the following results are obtained: , >
Ash Water White Water Wastewater
Analysis Parameter 5-9-72 5-9-72 5-9-72
pH 9.45 5.22 5.20
5 Day BOD - 9200 5150
Total Solids, mg/1 13176 10056 7820
Total Volatile Solids, mg/1 1710
Total Dissolved Solids, ng/1 2303 3090 3244
Total Settleable Solids, mg/1 11267 2451 2913
Thank you for this opportunity to be of service.
, ~, . Respectfully submitted,
2- File BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Division
194-
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LABORATORY REPORT
M.y 1, 1972
Report to: A. M, Kinney, Inc. - Consulting Engineers -
2912 Vernon Place - Cincinnati, Ohio 45219
Attn: Mr. Carl Miller
Report on: Four (4) Samples Submitted for Analysis
Laboratory No.
Authorization:
760280
604
The three (3) water samples and one (1) sand sample were received on April 10,
from Mr. Wayne Okel. These samples have the following identifications and required
analyses:
Ash Water (4-10-72) for
Wastewater (4-10-72) for
Whitewater (4-10-72) for
pH
Total Volatile Solids
Total Solids
Total Dissolved Solids
Total Settleable Solids
pH
5 Day EOD
Total Solids
Total Dissolved Solids
Toial Settleable Solids
pH
5 Day BOD
Total Solids
Total Dissolved Solids
Total Settleable Solids
Reactor Sand (4-10-72) for
Sieve Analysis
Silica Content
The above water standards were analyzed in accordance with procedures outlined in
Standard Methods for Water and Wastewater, 13th Edition, 1971. The sieve analysis of th
reactor sand was obtained using procedures in accordance with ASTM (D-1140)t Volume 11,
1970 Edition. The silica content of the sand was obtained using a wet chemical filtrati
method. The results of these analyses are as follows:
Water Analysis
PH
5 Day BOD
Total Solids, mg/1
Total Volatile Solids, mg/1
Total Dissolved Solids, mg/1
Ash Water
4-10-72
8,82
9367
909
2202
Wasfcewater
4-1G-72
5.07
3150
5936
2048
Whitewater
A-10-72
5.71
850
3113
1126
(continued)
195
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A. M. Kinney, Inc.
I'ago 2
Lab. No. 760280
Ash' Water
4-10-72
Wastewater
4-10-72
779.3. 4260
Reactor Sand 4-10-72
76.40
Wt.Sand Retained (grams)
Whitewater
4-10-72
1313
0
17
26
35
53
64
74
112
215
476
741
912
940
947
951
100
98
97
96
94
93
92
88
78
50
22
4
1
0.8
0.3
% Sand Passing
Total Settleable Solids, mg/1
Sand Analysis:
Si02%
Sieve Number, US
1/2
3/8
4
5
6
8
10
12
16
20
30
40
50
60
70
80
Sample Wt. = 954 g
Thank you for this opportunity to be of service.
Respectfully submitted, '
BOWSER-MORNER Testing Laboratories, Inc.
V
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
3- Client
2- File
CWK/jm
196
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LABORATORY REPORT April 26> 19?2
Report to: A. M. Klnney, Inc. - Consulting En-,.aeers - Laboratory No. 760132
2912 Vernon Place - Cincinnati, Ohio 45219 Authorization:
Attn: Mr. Carl Miller
Report on: One (1) Sample of Refuse Submit-red for Proximate Analysis
The sample was received from Mr. Way.ia Okel on April 18, 1972. It has the following
identification and required analysis.
Bag "BD" for Proximate Analysis
The analysis was performed in accordance with ASTM D-271, Part 19, 1971 Edition. A
discussion of the actual procedures used in this analysis la included in our Report #75964C
The references for the proximate analysis are as follows:
Analysis Parameter Reference Temperature
Moisture ASTM D-271 (Section 8) 75°C
Ash ASTM D-271 (Section 11) 750°C
,'Matile Matter ASTM D-271 (Section 14) 950°C
-~xed Carbon ASTM D-271 (Section 17)
BTU/lb. ASTM D-271 (Sections 44 - 47)
The samples were placed in a beaker and dried at 75 C to determine the moisture
content. The dried sample was then placed in a blender and blendedTajs fii>ie as possible.
This homogeneous sample was put back into the oven and redried .at 75. C. The remaining
analysis was performed using the dried sample. The result of'this analysis is as follows:
Proximate Analysis Bag BD
Moisture, % 54.17
Ash, % 5.85
Volatile Matter, % 35.82
Fixed Carbon, % 4.16
BTU/lb. (dry) Trial 1 6542
BTU/lb. (dry) Trial 2 6602
BTU/lb. (dry) Average 6572
Thank you for this opportunity to be of service.
Respectfully submitted,
3- Client BOWSER-MORNER Testing Laboratories, Inc.
2- File
CWK/jm
_ . Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
197
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LABORATORY REPORT , ,ril 26, 1972
Report to: A. M, Kinney , Inc. - Consulting Engineers - U aoratory No. 760131
2912 Vernon Place - Cincinnati, Ohio 45219 Authorisation:
Attn: Mr. C. K. Miller
Report on: One ^ Sample of Waatawater Submitted for Analysis
The water sample was received from Mr. Wayne Okel on April 18, 1972. The sample
has tha fallowing identification and required analyses: ' "v " -—-•-- f
/- f
Identification: A^al . ••••-....
Wastewater (4-18-72) for pJ -J ''.'372
5 Day BOD
Total Solids
Dissolved Solids
Settleable Solids
The above sample was analyzed in accordance with procedures outlined in Standard
Methods for Water and Wastewater, 13th Edition, 1971. Using these procedures the follow!
•esults were obtained:
Wastewater (4-10-72)
pH 6.06
5 Day BOD 2650
Total Solids, mg/1 8935
Dissolved Solids, mg/1 4506
Settleable Solids, mg/1 2917
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
3- Client
2- File
CWK/jm
198
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LABORATORY REPORT , ,,
April 14, 1972
Report to: A. M. Kinney, Inc. - Consulting inglneers - Laboratory No. 759642
2912 Vernon Place - Cincinnati s Ohio 45219 Authorization: 604
Attn: Mr. C. K. Miller
Report on: One (1) Sample of Refuse Submitted for Proximate Analysis
The sample was received from Mr. Wayne Jkel on April 10, 1972. It has the followin;
identification and required analysis:
Bag BC for Proximate Analysis
The analyses were performed in accordance with ASTM D-271, Part 19, 1971 Edition; a
discussion of the actual procedures used in this analysis are included in our Lab. Repori
No. 759640. The references for the proxiiuai_a analysis are as follows:
Analysis Parameter Reference Temperature
Moisture AS'.M D-27I (Section 8) 75°C
Ash ' ASTM D-271 (Section 11) 750°C
Volatile Matter ASTM D-271 (Section 14) 950°C
Fixed Carbon ASTM D-271 (Section 17)
BTU/lb. ASTM D-271 (Sections 44-47)
The samples were placed in a beaker and dried at 75°C to determine the moisture conl
The dried samples were then placed in a b leader and blended as fine as possible. The hoi
geneous sample was placed back in the oven and redried at 75°C. All of the remaining an<-
were determined using this dried sample. The results of these analyses are as follows:
Proximate Analysis 3C _
Moisture, % 52.80 /., T^ *- /
Ash, % 4.91 . .*
Volatile Matter, % 37.34 • '
Fixed Carbon, % 4.95
BTU/lb. (dry sample) Trial 1 7424
BTU/lb. (dry sample) Trial 2 7398
BTU/lb. (dry sample) Average 7411
Thank you for this opportunity to be of service.
Respectfully submitted,
Client - 3 BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
199
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LABORATORY REPORT' •• '• AIL,-^ %ft. 0
Vu . u i-.Afliill M, 19/2
Report to: A. M. Kinney, Inc. - Consulting Engineers — - Laboratory No. 759640
2912 Vernon Place - Cincinnati, Ohio 45219 * AutMrf&df
Attn: Mr. C. K. Miller
Report on: One (1) Sample of Refuse Submitted for Chemical Analysis
The following sample was received from Mr. Wayne Okel on March 7, 1972. This sample
has the following identification and required analysis:
Bag BIJ for Proximate, Ultimate and Complete Ash analysis
At the same time Mr. Okel requested that we recheck the analysis of bags AW and AY fc
chlorine, chlorides and sulfates, and that we should run a complete ash analysis on these
two samples.
The analyses were performed in accordance with ASTM Procedure D-271 (19), 1969 Editic
American Public Works Assocaition of Refuse, Appendix A; and Standard Methods, 13th Editic
1971. The analysis were performed as follows:
Proximate Analysis:
( 1.) Moisture ASTM D-271 (Section 8)
A portion of the sample is placed in a pre-weighed beaker and allowed to stand
In a oven at 75°C for 8 hours. The beaker is then removed from the oven, cooled
in a dessicator, and reweighed. The percent moisture is calculated from the fol
lowing equation:
«, Mn-f-i-nrp - (Wt' of Origlnal Sample - Wt. of Dry Sample)
A, Moisture Sample Weight X 1OU
2.) Ash Content ASTM D-271 (Section 11)
A known weight of part of the moisture dried sample is placed in a pre-weighed
porcelain crucible and placed in a muffle oven at 750°C. The crucible is left
in the oven for an hour, or until all of the initial sample is burned off and a
Iight-coio-"c1 asu is left. The crucible is then reraoved from the oven, put in a
dessicator, cooled, and reweighed. The percent ash is calculated from the fol-
lowing equation:
<7 A^V, - (Wt. of Ash) v inn
/£ Ash = -77 . 4 L = — X luU
(Corrected Sample Wt.
*. , c, -i TT - u^ (Vt. Sample for Ash) (Wt. . Sample for Moisture)
Corrected Sampla Weight = -* 1 -—-—. , e -g ,. . • r— e-
f & (tot. Residue from Moisture)
(continued)
200
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A. M. Kinney, Inc.
Page 2
Lab. No. 759640
3.) Volatile Matter ASTM D-271 (Section 14)
A portion of the dried sample is placed in a pre-weighed platinum crucible with
a lid. The weight of the sample ii obtained and the crucible is placed in a
muffle furnace at 95G°C for exac .. 7 minutes. The crucible is removed, placed
in a dessicatot, cooled, and rew^._g/_,j u The percent volatile matter is calculated
from the following equation;
Volatile Matter - • s*f*« ' Wt of Residue)
(Corrected Sample Wt.)
4.) Fixed Carbon ASTM D-271 (Section 17)
The fixed carbon is calculated fro® the following equation:
% Fixed Carbon = 100 - (% Moisture + % Ash + % Volatile Matter)
5.) BTU's ASTM D-271 (Sections 44-47)
The apparatus used in this procedure 13 a Paar Bomb Colorimeter. A ,5g portion
of the dried sample io placed in a stainless steel crucible, and set on the
supports stand of the bomb. The bomb is sealed and 250 psi of oxygen is added.
The bomb is ignited and the increase in temperature of the water jacket is noted.
The BTU/lb. is calculated from the following equation:
BTII/IK . (Benzoic Ag'd Factor) (AT)
BTU/lb. ----- (sample Wt/5 - -
Ultimate Analysis;
6.) Carbon APWA, Appendix A, Page 399
7 . ) Hydrogen
The carbon and hydrogen are run on an electrically heated organic combustion furnace.
A 1.0 gram portion of the dried sample is weighed directly into a combustion
crucible. The crucible is placed in the combustion tube of the furnace, and the
electric heaters are turned on. A flow of oxygen through the combustion tube is,
begun and the sample is heated for 30 minutes to allow for complete combustion.
Following this combustion the sample is kept in the tube with the oxygen still
flowing tc mahc. certain all of the water produced on ccabustion is carried to the
moisture absorption t"be . The percentages of carbon and of hydrogen are obtained
from the following equations:
„, _ . (Increase in Weight of C02 Absorption Bulb) (27.27)
A Carbon = -- "^-7; - : — rr — . * " ' •
Sample Wexght
% Hydrogen = (INCREASE in Weight of Moisture Absorption Bulb) (11.17)
Sample Weight
201
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A. M. Kinney, Inc.
Page 3
Lab. No. 759640
^ 8.) Oxygen ASTM D-271 (Section 42)
By definition, the oxygen content of the sample ie determined from the following
equation:
% Oxygen * 100 - (% Hydrogen + % Carbon •*- '':, ? Ltrc^en 4- 7. Sulfur -f % Ash . Moisture)
9.) Nitrogen ASTM D-271 (Sections 38-40)
The procedure used in this determination is the Kjeldahl-Gunning Method. A 1 g
sample is dissolved in 25 mis of 1:1 HC1 solution and is distilled in a Kjeldahl
flask. The distillate is collected in an Erlcnmeyer flask and is back titrated
with standard NaOH solution. The percent nitrogen present is calculated from the
following equation:
% Nitrogen - Carnality HpOH) (Vol. NaOH titrated) x ^
(Sample Wt.)
10.) Sulfur ASTM D-271 (Sections 22-23)
The procedure used in the sulfur determination is the bomb washing method. One of
the trials from the BTU determination is used. The contents of the bomb are washed
into a beaker with a methyl orange-water wash solution until no acid reaction occurs.
Ammonium hydroxide is added to the solution and it is filtered. Bromine water is
added to the filtrate and the sulfur is precipitated as BaS04 with the addition of
s-^ BaClz- The percent sulfur la calculated from the following equation:
„. (Wt. BaS04 precipitated) (13.74)
£ Sulfur = (Sample Wt.)
11.) Fluorine Orion Selective Ion Electrode
A 1.0 gram sample of the dried sample is p" acad ir. a beaker and treated with 50 mis
of distilled water. The solution is filteraa ana th2 filtrate is treated with a
buffer solution. The fluoride content Is chen determined on a pH meter using an
Orion selective ion tlc^-ide electrode. The fluorine content is then calculated
from this v.'iue for fluorido.
12.) Chlorine ASTM D-2361 (Sections 3-6) (Modified Procedure)
The chlorine content of the sample is determined using a Paar Bomb Colorimeter. A
0.8 gram sample of the dried material is placed in a stainless steel cup and
placed in the bomb containing 5 mis of sodium carbonate solution. The bomb is
sealed and 500 psi oxygen is pumped into it. The bomb is placed in the water
jacket --.id ignited. The contents of the bomb are washed Into a beaker, the
' solution is acidified and the chlorine is precipitated ec AgCl using AgN03 as a
reagent. The solution is allowed to set overnight in a dark place and is then
filtered th cough a pre-weighed sintered glass cr ;iciMe. The present chlorine
in the sample is calculated from the following equation:
202
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A. M. Kinney, Inc.
Page 4
Lab. No. 759640
% Chlorine - (Wt' ASC1 precipitated)
(Sample Wt.)
]'J.) Acid Soluble Aluminum - Perkin-Elmer Atomic Absorption ?~andbook
A 1.0 gram sample of the dried saciple is pl^, , .._:. •:. .esker and clasolvcc • :.
3.0 mis of HC1. The solution is filtered, anc thi- ill', -at;, is ccl:.fcc':^d _'. „.
100 ml volumetric flask. The flask is diluted to t"-2. -mark with distiiitc. .-..- •£•_•
and the concentration of aluminum is determined on &.;* atomic absorption opec.jo-
photometer using the absorbance technique. The acid soluble aluminum ip the
sample is reported in terms of A1203 content.
Ash Analysis;
14.) A1203 - Perkin-Elmer Atomic Absorption Handbook
Fe203 - Perkin-Elmer Atomic Absorption Handbook
CaO - Perkin-Elmer Atomic Absorption Handbook
MgO - Perkin-Elmer Atomic Absorption Handbook
K20 - Perkin-Elmer Atomic Absorption Handbook
Zinc - Perkin-Elmer Atomic Absorption Handbook
Lead - Perkin-Elmer Atomic Absorption Handbook
The metal oxides of the ash are determined by using a sodium fusion technique
on the atomic absorption spectrophotometer. A .25 g sample of the ash is ground
up in a morter and pestle and placed in a platinum crucible. Approximately 2 grams
of sodium carbonate is added, the crucible is covered, and heated over a Fisher
burner. When the sample in the crucible becomes a molten liquid the crucible is
removed from the burner and cooled. The cooled crucible is placed in a 1:1 HC1
solution until all of the fused material is dissolved. The solution is then
filtered into a 100 ml volumetric flask and the metal concentrations are determined
on an atomic absorption spectrophotometer. The filter paper is saved for the
Si02 determination. The oxides of the metala are calculated from these results
by multiplying the value for the ^lerjental determination by the appropriate gravi-
metric factor.
15.) Na20 Perkin-Elmer Atomic Absorption Handbook
A .5 gram sample of the ash is digested in 20 mis of HCl overnight. The solution
is then filtered into a 100 ml volumetric flask and is run on the atomic absorption
spectrophotometer as in the procedure above.
16.) Si02 Wet Chemical Method
The filter paper from the sodium fusion of the ash is placed in a platinum
crucible and ignited over a Fisher burner. After all the paper has been burned
off, the crucible is removed from the burner and allowed to cool. The crucible
and contents are weighed, 1 ml of H2S04 is added, and the contents are fumed in
HF under an evaporating coil. When all of the acid is evaporated off the
crucible is removed, allowed to cool, and reweighed. The loss in weight between
the two samples is the amount of S102 in the sample. The value is then multiplied
by 400 which gives tha % 81^9 ^ the
203
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A. M. Klnney, Inc. 1*%f*• *•' -•'" r&
Page 5 ~x
Lab. No. 759640
17.) Sulfoten Turbidometric TJ.tratlon with BaCl2
A ./ y, Hflmple of the ash la placed in a beaker and treated with 100 rals of wafer.
Aiu«r .U'lting thu solution set for an hour e known amount of Barium Chloride .In
added to precipitate 83804. The amount of BaSO/i in the sample is determined
measuring the cloudiness of the sample on a turbldometer, comparing the amount,
of cloudiness present to a blank deteraiuatXviu The % -sulfate is tV. _n e^cuU.-- i
by multiplying the result by the gravimetric, factor for ^ulfate.
18.) Chlorides Mercuric Chloride Titration
A .1 g sample is treated with 100 mis H20 and 2 mis Nitric acid and is filtered
into an Erlenmeyer flask. The amount of chloride present is determined by tit-
rating the solution with ^tandard mercuric nitrate solution and by performing
the appropriate calcv • IF
19.) Trace Metals SemiHjuautitative Determination by Emission Spectroscopy
The trace metals present in the ash are determined by using the technique of
powder burns on an emission spectrograph. A known weight of the ash is placed
in a vial and diluted with pure graphite and lithium carbonate to 300 rags. A
set of standard mixtures containing different amounts of trace metals is made
by the same method. Following this preparation of standard a fixed volume of
each sample and standard is placed in an individual graphite electrode cup and
is burned by a DC Arc source on the emission spectrograph. The relative con-
centrations of the metals in the sample are determined by coopering the density
of the spectra lines of the sample to those of the standards. The results are
reported as a range of values.
Using the above techniques the following results are obtained:
Sample Identification; AX AY BB
Proximate Analysis
Moisture, % 53.86 54.36 54.15
Ash, % 3.57 4.63 5.90
Volatiles, % 37.49 36.03 38.29
Fixed Carbon, % 5.08 4.98 1.66
BTU/lb. (dry sampleXTrial 1 8035 8300 8080
BTU/lb. (dry sample)Trial 2 8016 8391 8067
RTU/lb. (dry saraple)Average 8026 8345 8077
Sodium, % - .006
Silica, % - ' 1.51
204
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A. M. Kinney, Inc.
Page (»
Lob. No. 759640
Sample Identification;
Ultimate Analysis
Carbon
Hydrogen
Nitrogen
Oxygen
Sulfur
Chlorine, %
Fluorine, %
Acid Soluble Al
(as
Ash Analysis
Si02, %
A1203, 7.
CaO, %
MgO, %
AX
AY
BB
23.85
3.21
.026
Remainder
.13
.62
.05
1.10
22.90
2.84
.016
Remainder
.07
.35
.05
.79
22.45
2.76
.050
Remainder
.39
.31
.04
.76
1.
1.
.47
,23
.25
.09
.19
.02
.09
.005
.002
.058
1.65
1.78
.84
.23
.04
.10
.01
.05
.015
.010
.095
1.39
2.76
.82
.34
.10
.20
.01
.07
.009
.005
.068
1.42
Zinc, %
Lead, %
Chloridea, %
Sulfate, %
Trace Metals
Nickel
Titanium
Copper
Tin
Molybdenum
Lead
Manganese
The values for the proximate and ultimate determinations have been converted back to
a dry basis sample. The metal oxides in the ash analysis have been reported aa percent of
oxide present in the original sample. This value is obtained by multiplying the grams of
oxide present in the ash by the percentage of ash in the original sample. The trace metals
are reported in the same manner. However both the sulfate and chloride values are reported
as percentage of sulfate or chloride in the ash only.
.0025-. 0015
.015-. 05
.015-. 05
.0015-. 005
.0015-. 005
.005-. 01
.015-. 050
.0005-. 0025
.05-. 15
.025-. 10
.0005-. 005
.0005-. 005
.010-. 025
.025-. 05
.0005-.0025
.015-. 05
.015-. 05
.0025-. 005
.0025-. 005
.015-. 025
.025-. 15
205
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A. M. Kinney, Inc.
Page 7
Lab. No. 759640
In rmr rechccking of the data on camples AX and AY wo found that the values for
/itc ,ind chlorides that have been reported on previous reports were recorded ae parts
per million, and not percent. Also the previous analyses for chlorine were, In erroc, y-i
the use of bomb colorimetry in the chlorine determination gives a more accurate ard re-
producible result. I hope that the change in analytical procedures will rac,-^ Jhe
discrepancies in our prevoius work.
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Dlv.
3- Client
2- File
CWK/Jo
206
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LABORATORY REPORT
April 13, 1972
Report 10: A. M. Kinney, Inc. - Consulting Engineers -
2912 Vernon Place - Cincinnati, Ohio 45219
Attn: Mr. Carl Miller
Report on: TWO (2) Water Samples Submitted for A
Laboratory No. 759623
Authorization:
The two water samples were received from Mr. Wayne Okel on March 23, 1972. The
samples have the following identification and required analysis:
Identification:
Whitewater (3-23-72) for pH
~. Day BOD
Total Solids
Total Dissolved Solids
Settleable Solids
pH
5 Day BOD
Total Solids
Total Dissolved Solids
Settleable Solids
The above samples were analyzed in accordance with procedures outlined in Standard
Methods for Water and Wastewaters, 13th Edition, 1971. The settleable solids determinat
was run twice, once on a volume basis (results reported as ml/1) and once on a weight ba
(results reported as mg/1) as requested by Mr. Okel. The results of these analyses are
follows:
(3-23-72) (3-23-72)
White water Waatewater
Wastewater (3-23-72) for
pH
5 Day BOD, mg/1
Total Solids, mg/1
Total Dissolved Solids, mg/1
Settleable Solids, rag/1
Settleafale Solids, ml/1
5.20
3275
14,432
3897
9324
360
5.50
1225
6890
2040
4398
280
Thank you for this opportunity to be of service.
Respectfully submitted,
Client - 3
File - 2
CWX/jm
BOWSER-MORNER Testing laboratories , Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
207
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LAb^r,VTOnY REPORT
March 17, 19/2
Rcfortto: A. M. Kinney, Inc. - Consultlig Engineers - Laboratory No. 7:i8768
2912 Vernon ?lace - Cincinnati, Ohio 45219
Attn: Mr. C. K. Miller
Report on: Three (3) Watar Samples Submitted for Analysis Authorization:
The three (3) water samples you. received in two installments. The white water
and waste water samples were recei\r*.A. on March 1, 1972 a-td the ash water san-Ae was
received on March 7, 1972. These Sa.mpi-e& have •*;-'•.<, £0-'Lowing identification i.r^ re-
quired analysis.
White Water (3-1-72) for pH
5 D-v BOD
Total Solids
Dissolved Solids
Settleable Solids
Waste Water (3-1-72) for pH
5 Day BOD
Total Solids
Dissolved Solids
Settleable Solids
Ash Water (3-7-72) for pH
Total Solids
Volatile Solids
Dissolved Solids
Settleable Solids
• ? > x /
The above water samples were analyzed in accordance with'procedures outlined in
Standard Methods for Wastes and Wastewater, 13th Edition, J.971. The results of these
analysis were as follows:
White Water Waste Water Ash Water
Sample Identification; (3-1-72) (3-1-72) (3-7-72)
pH 5.40 6.10 8.65
5 Day BOD, tng/1 3,800 2,175
Total Solids, mg/1 15,294 6,969 20,997
Dissolved Solids, mg/1 5,131 4,716 3,049
Volatile Solids, mg/1 - - 2,680
Settleable Solids, ml/1 270 35 25
(continued)
208
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A. M. Kinney
Page 2
Lab. No. 758768
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
C-j-^e W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Dlv.
3- Client
2- File
CWK/jm
209
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LABORATORY REPORT February 23, 1972
Report to: A. Mt Kinney - Consulting Engineers - 2912 Vernon Laboratory No. 757947
Place - Cincinnati, Ohio 45219
Attn: Mr. Carlton Miller
Report on: Four (4) Sample3 Submitted for Analysis Authorization:
The following three water samples and one reactor sand saraple were received by
BOWSKR-MORNER on February 11, 1972. These c>ar,?l^ ;>avc the following idee: fi 'licauior,
and required analyses:
Ash Water (2-11-72) for pH
Volatile Solids
Suspended Solids
Dissolved Solids
Settleable Solids
^
White Water (2-11-72) for pH
5 Day LOD
Suspended Solids
Dissolved Solida
Settleable Solids
Waste Water (2-11-72) for pH
5 Day BOD
Suspended Solids
Dissolved Solids
Settleable Solids
Reactor Sand (2-11-72) for Sieve Analysis
Si02 Content
The above water samples were analyzed in accordance with procedures outlined in
Standard Methods for Waste and Wastewatar, 13th Edition, 1971. The sieve analysis of
the reactor sand was obtained using procedures in accordance x/ith ASTM (D-114Q) , Part 1
1970 Edition. The silica content of the sand was obtained using vret chemical filtratio
methods. The nsul'zs of. these analyses are as fellows:
(conti'aiad)
210
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A. M. KJnnc-y,
I'MRC* 2
l.ab. No. 757947
Waters:
PH
5 Day BOD, mg/1
Suspended Solids, mg/1
Dissolved Solids, mg/1
Settleable Solids, ml/1
Volatile Solids, mg/1
Reactor Sand:
Sieve Number^ US
3/8"
#4
95
#6
#8
#10
#12
#16
#20
#30
#40
#50
#60
Sample Size
Silicon Content
Ash Water Waste Water White Water
2-11-72 2-11-72
7.89
-
9700
3568
24
1513
Wt.
4.20
6050
f ]
— : - „/'
77.2
—
Sand Passing Sieve
Grains
0
37
57
82
161
220
290
488
714
890
999
1061
1071
2-11-72
4.73
7300
V "- ' ° "
• 3fcu
5CD.&
—
% Sand Passing Sie\'e
100
97
95
92
85
80
73
55
34
17
7
1
1
1076g
63.00 % S102
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Laboratory
Chemical & Metallurgical Division
3- Client
2- File
CWK/jm
211
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LABORATORY REPO for
pH -•- ' ;l ^'
Total Suspended Solids
Total V61a£i?2 Solids
Total Dissolved Solids
SettlGaV-.! Solids
Toial Soiids
pH
5 Day BOD
Total Suspended Solids
Total Dissolved Solids
Settleable Solids
Waste Water (1-19-72) for
PH
5 Day BOD
Total Suspended Solids
Total Dissolved Solids
Settleabla Solids
(continued)
-------
A. M. Kinncy, Inc.
Pago 2
Lab. No. 757334
Reactor Sand (1-19-72) for
Sieve Analysis
Silicon
The above water samples were analyzed in accordance with procedures outlined in
Standard Methods for Waste and Wastewater, 13th Edition, 1971. The sieve analysis cf
-rcawca v;.i.i ASTM (D-1I4C) , "c.__.
cb_«-;.ne;i using wet chemical
the reactor sand was obtained using procedures ±:.
11, 1970 Edition. The silicon content of ;he sand was
filtration methods. The results of these analyses areas follows:
Waters:
PH
5 Day BOD, mg/1
Total Solids, mg/1
Total Suspended Solids, mg/1
Total Dissolved Solids, mg/1
Total Volatile Solids, mg/1
Settleable Solids, al/1
Sieve Analysis:
Sieve Number, US
Combined
White + Ash
Wastewater Water
9-30-71 1-19-72
A.71
4400
7366
4884
3112
5407
6.50
16,398
10,728
2700
1184
30
Waste-
Water
1-19-72
7.39
1700
5160
270
85
White
Water
1-19-72
6.91
725
1070
580
210
Reactor Sand (1-19-72)
Wt. Sand Passing grans % Passing
Ash
Water
9-30-71
8.70
150
9301
9520
2108
1066
1/2
3/8
4
5
6
8
10
12
16
20
30
40
50
60
70
80
100
Pan
Sample Size 1077.0 g
0
5.0
122.0
177.0
239.0
334.0
382.0
431.0
548.0
692.0
827.0
941.0
1047.0
1067.0
1072.0
1073.0
1073.0
107.r..0
100.0
99.0
89.0
84.0
78.0
69.0
65.0
60.0
49.0
36.0
23.0
13.0
3.
1.
0.
0.4
0.4
0.3
.0
.0
.5
213
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A. M. Kinncy, Inc.
Page 3
Lab. No. 757334
S102, Z
Reactor Sand (1-19-72)
64.40
Thank you for this opportunity to be of service.
3- Client
2- Kile
CWK/Jm
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
214
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LABORATORY REPORT
February 16, 1972
Report to: A. M. Kinney, Inc. - Consulting Engineers - Laboratory No. 757726
2912 Vernon Place - Cincinnati, Ohio 45219
Attn: Mr. Carlton Miller
Report on: One (1) Refuse Sample Submitted for Chemical Authorization:
Analysis
The following sample was received frcra yo^r i':.r:i or. Ft-:.ruary 11, 1972. The _^:,I<
had the following identification:
Bag "BA" for Proximate Analysis only
The analyses were performed in accordance with ASTM Procedure D-271, Part 19, 196*
Edition; American Public Works Association of Refuse, Appendix A; and Standard Methods.
13th Edition, 1971. The analyses were performed as follows:
\
Proximate Analysis;
Analysis Parameter Procedure Tenperature
Moisture AFWA 75°C
Ash /jTM D-271 750°C
Volatile ASTM D-271 950°C
Fixed Carbon By Definition ASTM D-271
BTU/lb. Paar Bomb Colorimeter
The samples were placed in a beaker and dried at 75°C to determine the moisture
content. The dried samples were then placed in a blender and blended as fine as possit
This homogeneous sanple was placed back in the oven and redried at 75°C. The remaining
analyses were obtained from this dried sample. The results of these analyses are as
follows:
Proximate Analysis: "BA"
Moisture, % 52.19
Ash, % 4.78
Volatiles, % 38.33
Fixed Carbon, % 4.70
BTU/lb. (dry sample) Trial 1 77^1
BTU/lb. (dry sample) Trial 2 7720
BTU/lb. (dry sample; Average 7741
(continued)
215
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A. M. Kinney, Inc.
Page 2
Lab. No. 757726
Thank you for this opportunity to be of service.
3- Client
2- File
CWK/jm
Respectfully submitted,,
BOWiER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Laboratory
Chemical & Metallurgical Division
216
-------
\. M. Klniu-y, Inc.
I';W ')
l.;ib. No. 757325
The samples were placed in a beaker and dried at 75°C to determine the moisture
content. The dried samples were then placed in a blender and blended as fine as possible
This homogeneous sample was placed back in the oven and redried at 75°C. All of the re-
maining analysis were obtained from this dried sample. The ^2^3 content was determined
by fusing a portion of the ash residue with, sodium, carbonate. This fuse,! maso vc^ then
dissolved in hydrochloric acid and the amount of aluminum present was deterrii.vic by usiiv;
the solution technique on an atomic absorption spectrophotometer.
The results of these analyses are as follows:
Proximate:
Moisture, 7,
Ash, 7,
Volatile Matter, %
Fixed Carbon, %
BTU/lb. (Dry Sample) Trial 1
BTU/lb. (Dry Sample) Trial 2
BTU/lb. (Dry Sample) Average
UJ timntc:
Carbon, %
Hydrogen, %
Oxygen, 7,
Nitrogen, %
Sulfur, %
Chlorine, mg/1
Fluorine, mg/1
Total Aluminum (as
AW
52.31
5.19
37.99
4.51
8779
8806
8793
24.76
3.68
Rem.
.025
.27
.18
.03
.73
AX
53.86
3.57
37.49
5.08
8035
8016
8026
AX
23.85
3.2i
Rem.
.026
.13
.16
.05
.57
AY
54.36
4.63
36.03
4.98
8300
8391
8345
AY
22.90
2.84
Rem.
.016
.07
.09
.05
.68
AZ
51.84
5.72
38.41
4.03
8040
8076
8058
3- Client
2- File
SL/jm
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
v
iOO^vv^Ag ;\
Samuel Lncas, Jr.
Ma-jv.cr, Instrumentation Lab.
Che^i-cnl ?• .letallurgical Div.
218
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LA8CRATORY REPORT
December 30, 1971
Report to: A. M. Kinney, Inc. - Consulting Engineers -
2912 Vernon Place - Cincinnati, Ohio 45219
Attn: Mr. C. K. Miller
Report on: Three (3) Water Samples Submitted for Testing
Laboratory No. 756304
Authorization:
Waste Water (11-16-71) for
The three (3) water samples were received durir:,, ;_...„ v^ek. of November 1^
samples have the following identification and analysis required:
White Water (11-16-71) for pH
5 Day BOD
Total Suspended Solida
Total Dissolved Solids
Settleable Solids
PH
5 Day BOD
Total Suspended Solids
Total Dissolved Solids
Settleaole Solids
PH
Total Solids
Total Volatile Solids
Total Suspended Solids
Total Dissolved Solids
Settleable Solids
Ash Analysis and Trace Metals Present
The water samples were analyzed in accordance with Standard Methods for Water and
Wastewater, 13th Edition, 1971. The ash analysis of the ash water was performed on the
solid residue remaining after a portion of the water in the sample was evaporated. The
results of such analysis are as follows:
Water (11-16-71) for
PH
5 Day BOD, ng/1
Total Solids, mg/1
Total Suspended Solids, mg/1
Total Dissolved Solids, mg/1
Settleable Solids, ml/1
Total Volatile Solid, mg/i
White Water
11-16-71
5.41
3,370
7,244
6,403
300
Waste Water
11-16-71
6.18
3,100
776
',,016
9.5
Ash Water
11-16-71
10.19
19,432
16,856
2,244
10.2
1,098 .
(continued)
219
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A. M. kinney, Inc.
Page 2
Lab. No. 756304
AH)I An a lye Is;
S102, %
A1203, %
Fe203, 7,
CaO, %
MgO, %
NazO, %
K20, %
Sulfate, %
Zinc, %
Chloride, %
Lead, %
Trace Elements
Nickel
Silver
Copper
Tin
Molybdenum
Manganese
Chromium
Ash Water
11-16-71
Remainder
12.47
5.
9,
00
09
4.97
3.30
.96
1.22
.28
.387
.15
.01 - .05
.005 - .01
.25 - .50
.10 - .25
.001 - .005
.25 - .50
.01 - .05
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Laboratory
Chemical & Metallurgical Division
3- Client:
2- File
CWK/jm
220
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LABORATORY REPORT
December 3, 197:
Repon io: A. M. Kinney - Consulting Engineers - 2912 Vernorr
Flace - Cincinnati, Ohio 45219
A=tn: Mr. C. K. Miller
Report on: six (6) Samples Submitted for Chemical analysis
These samples were received during the weeks of Octobei
following identifications and analysis requested.
Laboratory No. 755476
Authorization:
3. The samples have the
Sample Identification:
Bag No.
Bag No,
Bag No.
Bag No.
Bag No.
1
3
A
5
13
Bags No. 12+20
Proximate -r Ultimate Analyses
Proximate 4- Ultimate Analysis
Proximate + Ultimate Analysis
Proximate -f Ultimate Analysis
Proximate + Ultimate Analysis
Proximate 4- Ultimate Analysis
Both the proximate and the ultimate analyses were performed in accordance with ASTM
Procedure D-271, Part 19, 1969 Edition; American Public Works Association of Refuse,
Appendix A; and Standard Methods, 13th Edition, 1971. The analyses were performed as
follows:
Proximate Analysis
Analysis Parameter
Moisture
Ash
Volatiles
Fixed Carbon
BTU/lb.
Ultimate Analysis
Analysis Parameter
Carbon
Hydrogen
Oxygen
Nitrogen
Sulfur
Fluorides
Chlorine
Total Aluminum
Procedure Temperature
APWA 75°C
ASTM-D-271 750°C
ASTM-D-271 950°C
By Definition ASTM-D-271
Paar Bomb Colorimeter
Procedure
APWA
APWA
Oxygen Determinator
APWA (Kjeldahl Method)
Paar Bomb Color-^eter + BaCl2 Precipitation
Mercuric: Nitrate Titration
Atomic Absorption Spectrophotometer
221
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A. M. Kittney
Page 2
Lab. No. 755476
The samples were placed loosely in a beaker and dried at 75°C to determine the
moisture content. The dried samples were then placed in a blender and blended as fine
as possible. At this point any pieces of foreign matter which had not been cut up were
removed and either cut or pulverized to the desired size. These samples were then redried
at 75° with all analyses except the moisture det..,rair..uiions being obtainec. fv., .. i.^c
sample.
The results of these analyses are as follows:
Proximate Analysis
Sample Identification;
Moisture, %
Ash, 7,
Volatiles, %
Fixed Carbon, %
BTU/lb. (Dry Sample) Trial 1
BTU/lb. (Dry Sample) Trial 2
BTU/lb. (Dry Sample) Average
Ultimate Analysis
Identification;
Carbon, %
Hydrogen, %
Oxygen, %
Nitrogen, %
Sulfur, %
Fluorides, mg/1
Chlorine, mg/1
Total Aluminum, %
Total Al (reported as
A1203)
Bag #1 Bag #3 Bap, #4 Bag #5 Bag #13 Bag # 12+20
49.37
4.04
40.14
6.45
7938
7833
7886
67.80
2.79
26.18
3.23
7137
7183
7160
65.10
2.90
28.62
3.38
8033
8007
8020
51.23
5.31
37.52
5.94
7176
7066
7121
57.35
4.29
33.40
4.96
7518
7582
7550
52.02
5.06
37.29
5.63
6846
6845
6846
Bag //I Bag //3 Bag 04 Bag #5 Bag 013 Bag #12+20
30.68
2.75
Rem.
0.21
0.24
0.01
0.09
0.26
0.49
27.68
3.02
Rem.
0.15
0.07
0.008
0.15
0.14
0.26
25.76
3.50
Rem.
0.37
0.27
0.007
0.19
0,16
0.30
33.72
2.68
Rem.
0.18
0.13
0.015
0.11
0.38
0.72
29.56
3.76
Rem.
0.25
0.38
0.005
0.17
0.24
0.47
31.41
1.95
Rem.
0.17
0.12
0.011
0.10
0.36
0.68
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
3- Client
2- File
SL/jp
Samuel Lucas, Jr.
Manager, Instrumentation Lab.
Chemical & Metallurgical Div.
222
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LABORATORY REPORT v nf
November 26, 1971
Report to: A. M. Kinney, Inc. - Consulting Engineers - Laboratory No. 755253
2912 Vernon Place - Cincinnati, Ohio 45219
Attn: Mr. C. K. Miller
Report on: Eight (8) Samples Submitted for Chc.iai.cal Anal/--:.':: -•.-ithorization:
Samples were received over a period of time for proximate analysis. The samples u&ve
the following identification:
Identification: ' Analysis
Bag No. AL Proximate Analysis Only
Bag No. AK Proximate Analysis Only
Bag No. AM ' Proximate Analysis Only
Bag No. AN Proximate Analysis Only
Bag No. AO Proximate Analysis Only
Bag No. AP Proximate Analysis Only
Bag No. AQ Proximate Analysis Only
Bag No. AR Proximate Analysis Only
The proximate analysis was performed in accordance with ASTM Procedure D-271, Part 19,
969 Edition; American Public Works Association of Refuse, Appendix A; and Standard Methods
3th Edition, 1971. The analysis were performed as follows:
Analysis Parameter Procedure Temperature (°C)
>
Moisture APWA 75°
Ash ASTM D-271 750°
Volatile Matter ASTM D-271 900°
Fixed Carbon By Definition ASTM D-271
BTU/lb. Paar Bomb Colorimeter
The samples were placed loosely in a beaker and dried at 75°C for the moisture content.
The dried samples were then placed in a Waring Blender and blended as fine as possible. The
samples were then redried at 75° and all analyses except the moisture determinations were
obtained using the dried sample.
The results of the analysis were as follows:
s s s
Sample No. AK AL AM AN
Moisture, % 52.58 57.19 49.08 47.08
Ash, % 4.22 3.58 4.21 6.11
Volatile Matter, % 31.j3 39.10 39.39 41.37
Fixed Carbon, % , 11.87 .13 7.32 5.44
(continued)
223
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A. M. Kinney, Inc.
Page 2
Lab. No. 755253
Sample No.
BTU/lb. (dry sample) Trial 1
BTU/lb. (dry sample ) Trial 2
BfU/lb. (dry sample) Average
Sample No.
Moisture, %
Ash, %
Volatile Matter, %
Fixed Carbon, %
BTU/lb. (dry sample ) Trial 1
BTU/lb. (dry sample ) Trial 2
BTU/lb. (dry sample ) Average
AL
AL
8000
3C37
AQ
50.56
5.10
39.54
4.80
8308
8194
8281
6744
8805
6773
AP
53.79
5.85
36.32
4.04
8554
8552
8553
AM
9083
9031
90S?
AQ
53.53
3.67
39.19
3.61
8152
8238
8195
AN
7607
7655
7631
AR
52.59
4.16
38.66
4.59
8189
8130
8160
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Clyde W. Kayser
Chemist, Instrumentation Lab.
Chemical & Metallurgical Div.
3- Client
2- File
CWK/jp
224
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.A&ORATORY REPORT November 18, 1971
Report to: A( M> Kinney, Inc. - Consulting Engineers - 2912 Vernoa Place
Cincinnati, Ohio 45219 Attn: Mr. Carl Miller
Report on: ^Q (2) Samples Submitted for Analysis
Laboratory No.: 754982
Analysis of two (2) samples of sand were received for analysis. The samples were
identified as follows:
Identification :, Clear Sand
Reactor Sand
The samples were analyzed in accordance with Scott's Standard Methods; ASTM Vol.
1970 Edition, Atomic Absorption Spectrophotometer and Infrared Spectrophotometer Pro-
cedures.
The sieve analysis of the two sand samples was accomplished in accordance with AS
Procedure D 1140 Volume 11, 1970 Edition and utilizing specific size sieves. The resu
were as follows:
Sample No. Clear Sand Reactor Sand
Sieve No., US Wt. Retained % Passing Wt. Retained % P
3/8 0 100.00 0 100
4 0 100.00 51.9 92.
8 0 100.00 125.3 82.
20 43.0 94.04 267.4 62.
30 246.1 65.85 344.4 51.
40 571.4 20.71 471.8 33.
50 621.0 13.83 636.9 9.6
70 690.8 4.14 696.8 1.1
100 714.8 0.81 703.4 0.2
270 720.0 0.09 704.0 0.1
325 720.0 0.09 704.1 0.1
Pan 720.0 0.09 704.6 0.0
Sample Size, gms 720.6 705.1
The chemical analysis of the samples were accomplished in accordance with Scott's
Standard Methods Volumes 1 and 2 aad Atcaic Absorption Spectrophotometer Procedures.
results of the analysis x^ere as follows.
(continued)
225
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A. M. Kinney, Inc.
Page 2
Lab. No. 754982
Sample No. Clear Sand Reactor Sand
S102, % 94.76 70.76
Loss on Ignition, % {. „ .;0 0.16
Moisture, % o.;j 0.37
Sulfur, % O.G06 0.033
P205, % 0.014 0.316
CaO, % 0.42 8.68
MgO, % 0.07 12.93
Fe203, % 0.54 2.12
A1203, % 0.38 4.91
All data is reported on dry basis.
The glass content of the materials were analyzed by Infrared and indices of refraction.
The results of the analysis indicate the following.
Clear Sand Index of Refraction Approximate Concentration
Quartz 1.5442 69.5
Chalcedony 1.531 . 30.5
Total 100.0
The a,, and 0 quartz are the major concentration with the breakdown being as follows:
a Quartz, % 75
6 Quartz 10
a Tridymite 10
3 Tridymite 3
a Cristobalite 2
Total 100.0
The reactor sand results are as follows:
Index of Refraction Approximate Concentration
Quartz 1.5439 47.0
Chalcedony 1.539 53.0
Total 100.0
a Quartz % 40
6 Quartz, % 20
a Tridymite 17
B Tridymite 8
a Cristobalite 10
8 Cristobalite 5
100.0
226
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A. M. Kinney, Inc.
Page 3
Lab. No. 754982
The chalcedony of the clear and reactor sand are composed of the following break-
down.
Clear Sand Reactor Sand
Hematite Fe203 43.5 54.0
Anorthite CaAl2Si20s 22.0 6*5
Enstatite MgSlOs 9.5 14,8
Mullite Al6Si2013 25.0 24.7
Total 100.0 100.0
Determining the glass content of the clear and reactor sand Is extremely difficult
and the best estimates are that any glass in the sample would be as follows:
Sample No. Glass, % Index of Refraction
Clear Sand Trace (< 0.5) 1.52 - 1.53
Reactor Sand 1.0 1.54 - 1.55
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
. va^-
Robert S. Jenkins
Manager, Organic Chemistry Lab.
Chemical & Metallurgical Div.
3- Client
2- File
RSJ/jp
227
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LABORATORY REPORT A , „. ,_,<
October 20, 1971
Report to: A> M. Kinney, Inc. - Consulting Engineers - Laboratory No. 753750
2912 Vernon Place - Cincinnati, Ohio 45219
Attn: Mr. C. K. Miller
Report on: Analysis of Three (3) Residue Samples Authorization:
Three (3) residue samples were received for analysis. The samples and analysis
requested were Identified as follows:
Sample No. Analysis
Pulp Screened and Organic Rejects Proximate and Ultimate
Pulp Unscreened and Organic Rejects Proximate and Ultimate
Screen Rejects Proximate and Ultimate
The proximate and ultimate analysis were performed in accordance with ASTM Procedure
D 271, and American Public Works Association of Refuse, Appendix A. The analysis were
performed as follows:
Analysis Parameter Procedure
.joisture APWA
Ash . ASTM D 271
Volatiles ASTM D 271
Fixed Carbon Definition ASTM D 271
BTU Parr Bomb Colorimeter
Carbon ASTM D 271
Hydrogen ASTM D 271
Oxygen Definition ASTM D 271
Nitrogen • Kjeldahl
Sulfur Sulfur Analyzer
Fluorine SPADNS Determination
Chlorine Mercuric Nitrate
Aluminum Atomic Absorption
The results of the analysis were as follows:
Sample No. Pulp Pulp Screen
Scroer.ed Unscreened Rejects
Moisture, % 75.07 78.19 30.59
Volatiles, % 21.45 18.66 32.39
Ash, % 0.65 1.96 5.80
Fixed Carbon 2.83 1.19 31.22
228
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A. M. Kinney, Inc.
Paj>e 2
Lab. No. 753750
Sample No.
BTU (Dry Sample), BTU/lb.
BTU (Dry Sample), BTU/lb.
BTU Average, BTU/lb.
Carbon, %
Hydrogen, %
Oxygen, %
Nitrogen, %
Sulfur, %
Fluorine, mg/1
Chlorine, mg/1
Aluminum, mg/1
Pulp
Screened
8930
9005
8967
8.71
1.20
Remainder
0.41
0.18
0.06
0.08
0.59
Pulp
Unscreened
9356
9397
9377
9.85
0.91
Remainder
0.15 '
0.09
0.02
0.07
0.38
Screen
Rejects
5466
5.
Remainde
0.37
0.25
0.09
0.19
0.96
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-KORNER Testing Laboratories, Inc.
Robert S. Jenkins
Manager, Organic Chemistry Laboratory
Chemical & Metallurgical Division
Client - 3
File - 2
RSJ/jp
229
-------
LABORATORY REPORT
Report to: A. M. KJ.nney, Inc. - Consulting Engineers -
2912 Vernon Place - Cincinnati, Ohio 45219
Report on: Analysis of Residue Samples
October 1, 1971
Laboratory No. 753127
Authorization:
Samples were received periodically for-Proximate and Ultimate analysis. The samp
nnd analysis were identified and performed as follows:
Identification:
Analysis Requested
Sample No.
SampJe No.
Sample No.
Sample No.
SnmplR No.
Sample No.
Sample No.
Sample No.
Sample No.
Sample No.
Sample No.
Sand
W
X
Y
Z
AA
AB
AC
AD
AE
AF
AG
Proximate and Ultimate
Proximate
Proximate
Proximate and Ultimate
Proximate and Ultimate
Proximate
Proximate and Ultimate
Proximate and Ultimate
Proximate
Proximate
Proximate
Sieve Analysis
230
-------
A. M. Kinney, Inc.
Page 2
Lab. No, 753127
Identification; Analysis Requested
Water Samples pH, BOD and Solids
The proximate and ultimate analysis were performed in accordance with ASTM Pkc^c^-ri
D-271, Part 19, 1969 Edition, American Public Works Association of Refuse, Appendix A
and Standard Methods, 13th Edition, 1971. The analysis were performed as follows:
Analysis Parameter Procedure Temperature, °C
Moisture APWA 75
Ash ASTM D-271 750
Volatiles ASTM D-271 950
Fixed Carbon Definition ASTM D-271
BTU Parr Bomb Colorimeter
Carbon ASTM D-271
Hydrogen ASTM D-271
Oxygen Definition ASTM D-271
Nitrogen KJeldahl
Sulfur Sulfur Analyzer
Fluorine SPADNS Determination
Chlorine Mercuric Nitrate
Aluminum Atomic Absorption
BOD Standard Methods, 13th Ed, 1971
Solids StauJavJ Methods, 13th Ed., 1971
The samples were placed loosely in a container and dried at 75°C. The dried samples
were placed in a Waring Blender and blended as fine as possible. The samples were then
redried at 75°C and all analysis except moisture analyzed on the dried sample.
The results of the analysis were as follows:
231
-------
A. M. Kinriey, Inc.
Page 4
Lab. No. 753127
Sample No. w X Y Z AA AB AC
CaO
MgO
K20
Sulfate, S04, mg/1
7inc as Zn
chloride
Lead as ?b
Moisture, % 45.07 44.93 53.07 49.51 49.66 51.09 49.9"
44.5 44.86 52.53 *
Volatiles, % 43.86 43.34 37.49 39.09 38.10 37.34 38.71
Ash, % 5.37 5.31 4,37 5^3 3885 5.15 ft.'-V
Fixed Carbon, % 6.23 6.49 5.61 A,. V 3.61 i.06 • >-,.
BTU (Dry Sample) 7754 7736 7457 7166 7406 12B 72,.5
BTU (Dry Sample) 7671 7721 7487 7203 7533 7128 71* B
BTU Average 7713 7729 7472 7185 7470 7177 7152
Carbon, % 21.75 21.82 27.31 20.41
Hydrogen, % 2.04 3.52 4.75 1.76
Oxygen, % Hem. Rem. Rem. Rem,
Nitrogen, % 0.15 0.09 0.15 0.21
Sulfur, % 0.18 0.10 0.19 0.15
Fluorine, tag/1 0.03 0.08 0.07 0.08
Chlorine, mg/1 0.15 0.12 0.12 0.19
Aluminum, mg/1 0.65 .57 .64 0.30
Sample No. AD 0 P. AE AP AG
Moisture, % 56.53 53.09 54.83 54.17 56.26 51.89
Volatiles, % 33.09 35.88 35.49 33.59 32.77 38.42
Ash, % 5.67 4.91 5.00 6.83 5.36 5.76
Fixed Carbon, % 4.71 6.12 4.68 5.41 5.61 3.92
BTU (Dry Sample) 7047 - - 7397 7371 7099
BTU (Dry Sample) 7196 - - 7477 7234 6933
BTU Average 7122 - - 7437 7303 7016
ASH ANALYSIS,
Sample No.
Si02
A1203
Remainder
.86
.20
.082
.089
.15
.072
48.0
.004
2.13
.003
Remainder
.39
.18
.08
.07
.12
.05
68.5
.001
2.13
.001
Remainder
.07
.028
.011
.011
.018
.006
43.5
.001
66.4
.001
232
-------
A. M. Kinney, Inc.
Page 5
Lab. No. 753127
The sand sample was submitted to gradation after oven drying 637 grams and washing
over a No. 325 Sieve and redrylng and then mechanically shaken to give the following result
Sieve Size (U.S.) % Finer by Weight
" 3/8" 100
#4 98
#5 97
#6 96
#8 94
//10 93
//12 91
#16 88
020 82
#30 70
#40 44
#50 14
#60 5
#70 2
#80 0.8
#100 0.6
#140 0.5
#200 0.5
#270 0.3
#325 0.3
233
-------
A. M. Kinney, Inc.
Page 6
Lab. No. 753127
The water samples were analyzed in accordance with Standard Methods for Water and
Wastewater, 13th Edition, 1971 with the following results:
Sample Mo^ Ash* Write Wasiui
pH 9.30 5,10 5.10
5 Day BOD, mg/1 - > 1540 > 1460
Total Solids, mg/1 11,922
Total Volatile Solids, mg/1 1,448
Total Suspended Solids, mg/1 15,410 4,020 4,800
Total Dissolved Solids, mg/1 2,960 2,250 2,480
Settleable Solids, ml/1 28 240 210
* The ash sample had sand present and was therefore impossible to get representative
sample.
Thank you for this opportunity to be of service.
Respectfully submitted,
BOWSER-MORNER Testing Laboratories, Inc.
Edward W. Brirkuth, Vice-President
Director, Chemical & Metallurgical Division
Client - 3
File - 2
EWD/jp
234
-------
APPENDIX B - A. M. KINNEY, INC., TEST REPORTS
(30 PAGES)
235
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
DATE:
COLLECTED BY:
ANALYZED BY:
August 14, 1972
N. W. Okel DATE: August 2, 1972
N. W. Okel
MAGNETIC FRACTION:
WEIGHT OF SAMPLE:
ALL STEEL CANS:
STEEL CANS/ALUMINUM TOPS:
OTHER MAGNETIC MATERIALS:
DESCRIPTION:
UNACCOUNTED FOR:
11.22 pounds
50. OZ
10.6Z
37.6Z
Wire, nails, tools, door hardware
1.8Z
236
-------
MIXED SAMPLE MAGNETIC FRACTION
8.2.72
STEEL CANS FRACTION
8.2.72
237
-------
REPORT OF ANALYSIS OF JUNX REMOVER REJECTS
NOU-MAGNETIC FRACTION:
SIZE SAMPLE:
MOISTURE:
ORGANICS:
MAGNETIC METALS:
ALUMINUM:
OTHER METALS:
GLASS:
RUBBER MATERIALS:
PLASTICS:
OTHER:
DESCRIPTION:
11.82 pounds
13.0% free H20
N.D.%
0%
7.72
11.1%
31.5%
10.8%
4.6%
23.7% includes organic
Paper, wood, ceramics, stones
238
-------
JUNK REMOVER REJECTS
239
-------
240
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
DATE July 10, 1972
COLLECTED BY: N. W. Okel DATE: July 6, 1972
ANALYZED BY: N. W. Okel
MAGNETIC FRACTION:
WEIGHT OF SAMPLE: 18.42 pounds
ALL STEEL CANS: 69.3%
STEEL CANS/ALUMINUM TOPS: 5.7%
OTHER MAGNETIC MATERIALS: 24.3Z
241
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
NON-MAGNETIC FRACTION:
SIZE SAMPLE:
MOISTURE:
ORGANICS:
MAGNETIC METALS:
ALUMINUM:
OTHER METALS:
GLASS
RUBBER MATERIALS:
PLASTICS:
OTHER:
DESCRIPTION:
UNACCOUNTED FOR:
(July 6, 1972)
13.2 pounds
N.D.%
N.D.% very low
1.1%
4.4%
4.2%
37.0%
2.8%
0.8%
48.5%
Mostly large stones and gravel
1.2%
242
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
DATE:
COLLECTED BY:
ANALYZED BY:
June 21, 1972
N. W. Okel DATE: June 8, 1972
N. W. Okel
MAGNETIC FRACTION:
WEIGHT OF SAMPLE:
ALL STEEL CANS:
STEEL CANS/ALUMINUM TOPS:
OTHER
DESCRIPTION:
NONMAGNETIC MATERIALS
AND WATER:
22.39 pounds
67.1%
3.5%
26.4%
Heavy gage sheet metal, wire,
nails, etc.
3.0%
243
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
NON-MAGNETIC FRACTION:
SIZE SAMPLE:
MOISTURE:
ORGANICS:
MAGNETIC METALS:
ALUMINUM:
OTHER METALS:
GLASS:
RUBBER MATERIALS:
PLASTICS:
OTHER:
DESCRIPTION:
(Sample June 8, 1972)
12.33 pounds
8.4%
42.4%*
2.8%
9.6%
1.3%
23.2%
7.4%
4.9%
*%
*0rganics includes other materials
such as stones, ceramics, etc.
244
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
DATE:
COLLECTED BY:
ANALYZED BY:
May 15, 1972
N. W. Okel DATE: May 2, 1972
N. W. Okel
MAGNETIC FRACTION:
WEIGHT OF SAMPLE:
ALL STEEL CANS:
STEEL CANS/ALUMINUM TOPS:
OTHER
DESCRIPTION:
WATER AND UNACCOUNTED FOR:
(RAGS, PAPER, OTHER NON-
MAGNETIC MATERIAL)
41.05 pounds
67.6%
2.4%
27.4%
Automobile oil filters (2),
wire, nails, etc.
2.6%
245
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
NON-MAGNETIC FRACTION:
SIZE SAMPLE: 14.16 pounds
MOISTURE: 0% free
ORGANICS: 66.3%
MAGNETIC METALS: 0.8%
ALUMINUM: 10.2%
OTHER METALS: 2.5%
GLASS: 7.4%
RUBBER MATERIALS: 8.0%
PLASTICS: 4.4%
OTHER: 0.4%
DESCRIPTION: Unaccounted for
NOTE: No free water present. However organic fraction very wet -
probably 50% to 60% moisture.
Samples taken after Hydrapulper had been out of service for
broken motor shaft. May account for high organic content.
246
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
DATE:
COLLECTED BY:
ANALYZED BY:
REMARKS:
March 28, 1972
N. W. Okel DATE:
N. W. Okel
Free water - 23%
March 23, 1972
MAGNETIC FRACTION:
WEIGHT OF SAMPLE:
ALL STEEL CANS:
STEEL CANS/ALUMINUM TOPS:
OTHER MAGNETIC MATERIALS:
DESCRIPTION:
NONMAGNETIC MATERIAL:
UNACCOUNTED FOR;
15.70 pounds (dry)
75.0%
10.5%
12.5%
Wire, nails, miscellaneous
unidentifiable
1.02%
0.98%
247
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
NON-MAGNETIC FRACTION:
SIZE SAMPLE:
FREE MOISTURE:
ORGANICS:
MAGNETIC METALS:
ALUMINUM:
OTHER METALS:
GLASS:
RUBBER MATERIALS:
PLASTICS:
UNACCOUNTED FOR:
DESCRIPTION:
13.84 pounds
11.6%
3.0%
7.5%
39.3%
8.0%
4.2%
0.1%
"Organics" include other material
such as stones, ceramics, etc.
NOTE: Organics and moisture not determined by heating. Size of material
too large to obtain representative small sample.
248
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
DATE:
COLLECTED BY:
ANALYZED BY:
REMARKS:
March 7, 1972
N. W. Okel DATE: February 17, 1972
N. W. Okel
Free water prudent "5.1%
MAGNETIC FRACTION:
WEIGHT OF SAMPLE:
ALL STEEL CANS:
STEEL CANS/ALUMINUM TOPS:
OTHER:
DESCRIPTION:
NON-MAGNETIC MATERIAL:
21.05 pounds (air dry)
85.7%
2.31
9.2%
Wire, nails, small hardware
1.62+
NOTE: Non-magnetic material mainly organics and plastic, and percent
reported is that which could be easily separated.
249
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
SAMPLE DATE:
NON-MAGNETIC FRACTION:
SIZE SAMPLE:
MOISTURE:
ORGANICS:
MAGNETIC METALS:
ALUMINUM:
OTHER METALS:
GLASS:
RUBBER MATERIALS:
PLASTICS:
UNACCOUNTED FOR:
DESCRIPTION:
February 17, 1972
14.23 pounds
N.D.% (atr dried)
50.8%
1.5%
10.6%
6.0% (including 1.22 Cal. Bui.)
12.7%
11.6%
5.5%
1.3%
"Organics" contains "other materials"
such as:
Ceramics
Stones
Wood
Paper
Etc.
NOTE: Organics and moisture not determined by heating. Size of fractions too
large to obtain representative small sample.
250
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
DATE:
COLLECTED BY:
ANALYZED BY:
January 31, 1972
N. W. Okel DATE: January 25, 1972
Ron ReInking
MAGNETIC FRACTION:
WEIGHT OF SAMPLE:
ALL STEEL CANS:
STEEL CANS/ALUMINUM TOPS:
OTHER
DESCRIPTION:
25.32 pounds
72.3%
7.2%
20.4%
Automotive parts, nuts, bolts, wire
251
-------
REPORT OF ANALYSIS OF JUNK REMOVER REJECTS
NON-MAGNETIC FRACTION:
SIZE SAMPLE: 595.5 grama
MOISTURE: 22.5%
ORGANICS: 10,2% O.D. basis
MAGNETIC METALS: 0.3% 0,D. basis
ALUMINUM: 2.3% O.D. basis
OTHER METALS: 4.2% O.D. basis
GLASS: 63.8% O.D. basis
RUBBER MATERIALS: 6.5% O.D. basis
PLASTICS: 1.1% O.D. basis
OTHER: (INCLUDING ORGANICS) 21.9% O.D. basis
DESCRIPTION: Wood, rocks,fibrous material,
orgaaics, etc.
252
-------
REPORT ON ANALYSIS OF LIQUID CYCLONE REJECTS
DATE: August 16, 1972
COLLECTED BY: N. W. Okel DATE: August 2, 1972
ANALYZED BY: N. W. Okel
RESULTS:
MOISTURE: 19.6%
ORCANICS: 3.1%
LESS THAN NO. 10 SIZE: 9.4%
RETAINED ON NO. 10: 21.6%
RETAINED ON ON. 4: 69.0%
COMPOSITION OF MATERIAL RETAINED ON NO. 4 AND 10
CLEAR GLASS: 46.8% of total dry
GREEN GLASS: 6.7% of total dry
AMBER GLASS: 19.4% of total dry
MAGNETIC METALS: 1.7% of total dry
ALUMINUM: 0.8% of total dry
OTHER METALS: 1.5% of total dry
LARGE STONES: 3.1% of total dry
UNCLASSIFIED: 20.0% of total dry
(CERAMICS, WOOD, PAPER,
BONES, PLASTICS, RUBBER)
253
-------
254
-------
255
-------
0 i
8 9
MM
I
S 9
256
-------
''
r
'
I c. . .
'
1
2, ;
'I1
5 <
•I1
'!'
'I1
i 5 S
1
1
' t
'!'
$ 5
INCHES
C'r,
'I'gfH
i 2
' I I
345
INCHES
11 T j-rrrrrrrp] '"if,
s 7 ft t 'f
CYCIONt REJECTS
. JMAGNt !1C METALS f RACTION
257
-------
r|(
'
i i
45
INCHES
CYCLONfc REJECTS
ALUMINUM Hi ACTION
n
"riTI-'r 'I1 '!'
s I 1
I t
INCHES
CYCLONE REJECTS
OTHER METALS FRACTION
258
-------
PT1'!
I Z3
4567
INCHES
891
CYCLONE" REJECTS
STONES
I ! I
259
-------
REPORT ON ANALYSIS OF LIQUID CYCLONE REJECTS
DATE:; July 10, 1972
COLLECTED BY: N. W. Okel DATE: July 6, 1972
ANALYZED BY: N. W. Okel
RESULTS:
MOISTURE: 20.2%
ORGANICS: 3.9%
LESS THAN NO. 10 SIZE: 8.3%
RETAINED ON NO. 10: 23.9%
RETAINED ON NO. 4: 67.8%
COMPOSITION OF MATERIAL RETAINED ON NO. 4 AND 10
CLEAR GLASS: 40.1% of dry fraction
GREEN GLASS: 4.8% of dry fraction
AMBER GLASS: 18.1% of dry fraction
MAGNETIC METALS: 2.3% of dry fraction
ALUMINUM: 3.0% of dry fraction
OTHER METALS: 0.2% of dry fraction
LARGE STONKS: 4.3% of dry fraction
UNCLASSIFIED: 26.9% of dry fraction
UNACCOUNTED FOR: 0.3%
26G
-------
REPORT ON ANALYSIS OF LIQUID CYCLONE REJECTS
DATE: June 21, 1972
COLLECTED BY: N. W. Okel DATE: June 8, 1972
ANALYZED BY: N. W. Okel
RESULTS:
MOISTURE: 14.9%
ORGANICS: 10.1%
LESS THAN NO. 10 SIZE: 14.5%
RETAINED ON NO. 10: 23.0%
RETAINED ON NO. 4: 62.5%
COMPOSITION OF MATERIAL RETAINED ON NO. 4 AND 10
CLEAR GLASS: 34.5% of dry fraction
GREEN GLASS: 4.1% of dry fraction
AMBER GLASS: 19.5% of dry fraction
MAGNETIC METALS: 7.1% of dry fraction
ALUMINUM: 2.3% of dry fraction
OTHER METALS: 0.4% of dry fraction
LARGE STONES: 3.7% of dry fraction
•*
UNCLASSIFIED: 28.4% of dry fraction
261
-------
REPORT ON ANALYSIS OF LIQUID CYCLONE REJECTS
DATE: May 16, 1972
COLLECTED BY: N. W. Ok«l DATE: May 2, 1972
ANALYZED BY: N. W. Okel
REMARKS: Sample-: after Hydrapulpsr had been
down to replace broken motor shaft.
RESULT:
MOISTURE: 13.0%
ORGANICS: 13.6% dry
LESS THAN NO. 10 SIZE: 13.3% dry
RETAINED ON NO. 10: 24.3% dry
RETAINED ON NO. 4: 62.5% dry
COMPOSITION OF MATERIAL RETAINED ON NO. 4 AND 10
CLEAR GLASS: 38.1% of dry fraction
GREEN GLASS: 4.3% of dry fraction
AMBER GLASS: 14.7% of dry fraction
MAGNETIC METALS: 3.1% of dry fraction
ALUMINUM: 2.9% of dry fraction
OTHER METALS: 1.0% of dry fraction
LARGE STONES: 0% of dry fraction
UNCLASSIFIED: 35.9% of dry fraction
262
-------
REPORT ON ANALYSIS OF LIQUID CYCLONE REJECTS
DATE: March 8, 1972
COLLECTED BY: N. W. Okel DATE: March 1, 1972
ANALYZED BY: N. W. Okel
REMARKS: Percent composition is percent of
i-lO mesh fraction. It is also per-
cent of total if assumption that -10
mesh fraction is essentially the same
composition.
RESULTS:
MOISTURE: 15.25%
ORGANICS: (LOSS ON IGNITION)8.5% O.D. basis
LESS THAN NO. 10 SIZE: 10.0%
RETAINED ON NO. 10: 28.4%
RETAINED ON NO. 4: 62.0%
COMPOSITION OF MATERIAL RETAINED ON NO. 4 AND 10
CLEAR GLASS: 40.9% of +10 mesh O.D. basis
GREEN GLASS: , 5.9% of +10 mesh O.D. basis
AMBER GLASS: 18.0% of +10 mesh O.D. basis
MAGNETIC METALS: 4.1% of +10 mesh O.D. basis
ALUMINUM: 3.0% of +10 mesh O.D. basis
OTHER METALS: 1.1% of +10 mesh O.D. basis
LARGE STONES: 0.9% of +10 mesh O.D. basis
UNCLASSIFIED: 25.6% of +10 mesh O.D. basis
(INCLUDES ORGANICES,
STONES, PLASTICS,
RUBBER, ETC.)
263
-------
REPORT ON ANALYSIS OF LIQUID CYCLONE REJECTS
DATE: January 28, 1972
COLLECTED BY: N. W. Okal DATE: January 25, 1972
ANALYZED BY: Ron Reinking
REMARKS: Carbon residue present after
organics test
RESULTS:
MOISTURE: 14.4%
ORGANICS: 5.4%
LESS THAN NO. 10 SIZE: 12.7%
RETAINED ON NO. 10: 26.1%
RETAINED ON NO. 4: 61.5%
COMPOSITION OF MATERIAL RETAINED ON NO. 4 AND 10
CLEAR GLASS: 37.1% of total
GREEN GLASS: 4.5% of total
AMBER GLASS: 25.1% of total
MAGNETIC METALS: 2.7% of total
ALUMINUM: 2.0% of total
OTHER METALS: 0.3% of total
LARGE STONES: 6.8% of total
UNCLASSIFIED: 21.5% of total
264
-------
REPORT ON ANALYSIS OF LIQUID CYCLONE REJECTS
DATE:
COLLECTED BY:
ANALYZED BY:
REMARKS:
January 28, 1972
N. W. Okel DATE: January 19, 1972
Ron ReInking
Carbon residue left from burning
off organics.
RESULTS:
MOISTURE:
ORGANICS:
LESS THAN NO. 10 SIZE:
RETAINED ON NO. 10:
RETAINED ON NO. 4:
COMPOSITION OF MATERIAL RETAINED ON
CLEAR GLASS:
GREEN GLASS:
AMBER GLASS:
MAGNETIC METALS:
ALUMINUM:
OTHER METALS:
LARGE STONES:
UNCLASSIFIED:
(PLASTICS, CERAMICS,
WOOD, FIBERS, ETC.)
UNACCOUNTED FOR:
15.5%
4.2%
10.2% of dry sample
27.8% of dry sample
62.5% of dry sample
NO. 4 AND 10
37.4% of total
4.3% of total
22.4% of total
3.0% of total
2.0% of total
1.0% of total
6.2% of total
22.1% of total
1.6%
265
-------
APPENDIX C - THE BLACK CLAWSON COMPANY STATUS REPORTS
(102 PAGES)
266
-------
]-M?7\!!KT,:VN
1. OVKHATTMr- OAT A
J-'OH r.OUTi
JULY, 3.972
c—-
Tons v.'uicjhod
Tons SVd £ce vehicles
Tons total
Refuse Processed
Tonr,
% of received
Fiber Recovered
Tons, AD
% BOR
Tons Shipped
Korrov.r. Mr-tnl Recovered
Tons
% JiOR
Motf:v"j ol JjJ-indf •> 13.ed
Tour,, nonprocesssable
% ol received refuse
Tow; precis:;, residue
% of processed refuse
Klflocnt to MCD
Millions of. gallons
GPM
nlectricity
Total KWH
K\^]/Ton Processed
VJai-.or
Millions of gallons
GPI1
Gallons/ton
Opei'cil: ing Time
Days
Hours
Hydrnpulper
Reactor
Pi bred a in
July
Actual
792
64
856
830
97
25.8
3.1
0
65
7.8
26
3
121
14.6
1.8
255
151,000
181
2.3
325
2,780
20
117
110 .
46
Previous
Month
996
56
1,052
1,030
98
4.4
0.4
7
70
6.8
22
2
141
13.7
.5(
125
171,000
165
2.2
233
2,130
22
156
147
15
Desiqn
X,i6C
...
i,^i;
1,160
100
233
20
233
69
6.
0
0
108
9.
f//^'C/Jl^J
50
179, OOC
154
4
1C
1C
1C
267
-------
FRANKT.TN PLANT OPERATING REPORT FOR MONTH OF JULY, 1972
Page 2
Product ion Uotru
Hydrapulpcr, TPII
Reactor #/min.
Pibrcclaim TPII
Jxily
Actual
7.1
126
0.6
Previous
Month
6.6
120
0.3
Design
6.6
131
1.3
2. SAFETY
a) No accidents were reported in the month.
b) Unsafe operating in plant are:
1) Some pieces of equipment still need guards.
2) Floors are slippery in some areas.
c) Past plans and action.
1) Finish guards - not finished yet.
2) Layout trenches - nothing done.
d) P3?.ns for future.
1) Finish guards.
2) Layout crcnches or drain around compressors.
/
HOUSEKEEPING ' . "
a) Main housekeeping problems are:
1) Floor around magnetic conveyor.
2) Floor under conveyor and around air compressors.
3) Grates due to high sump level.
1>) Past: plans and action
1) Decign new shields around magnetic separator - tried some
new shields, helped a little.
2) Design rake for conveyor discharge or buy new hoppers under
conveyor - bought new hoppers/ will field fabricate rake.
3) Try new deodorants to combat odor-odor now under control.
c) Future P3.ans - . '
1) Fix Wc\tcr leak at water meter.
2) Order new pump for sump #122.
3) Field design and fabricate rake for conveyor.
268
-------
5,
PULP QUALITY AND PUODUCTION\ \
a) Grease extraction tests were made during Ouly to test clarifier
performance. Extractables ranged from 1.8% to 4.0% based on
pulp.
b) Past plans and action.
1) Shake down new equipment and determine yield. - New
equipment operates satisfactorily, however, yitld still
low due to loss at thickening equipment. Raising consistenc;
may help.
c) Future plans. . . :
1) Determine reason for low yield and fix.
OPERATION
Production Rate.
1) The Bydrapulper production rate was 7.1 tons/hour.
This is an B% increase over June.
2) Tho Kibrcclciim production rate averaged 0.6 ton/hour.
This is twice the rate of June, but still only 50% of design
3) The reactor operating rate was 126. #/min.
b) Problems
1) Stutors coming loose was a problem in July. A new extractio:
chamber will be installed in August, this should help.
2) The reactor cone and support is scheduled to be installed in
August. Also new refractory will be installed in the scrubb
inlet.
3) Yield is a problem in F'ibreclaim.
c) Maintenance (non routine)
1) The conveyor variable speed drive had a bearing go bad.
d) Power
Total power consumption for July was 151,000 KWH. This is 101
KWH/Ton which is 27 KWH/ton over design. The increase over June
is probably due to increased running time of Fibreclaim and its
increased Hp demand.
e) Labor 269
i overtime was considered normal for operations.
-------
J'l' l']i.'Vi:.l \'l I <:\./\ J. JL i\vi »\l -i yix I ) v.'; •« t i v. v j. I I \JL u v».<-. J
Paejr- 4 ...
5- O PIS RAT TON - Continued
I
f) Unv.uual costs.
No new unusual costs were incurred during the month.
6. SUMMARY
a) The stators on the pulper and .the conveyor drive were the
major problem in Hydrasposal. The rotor was not changed
during the entire month.
b) The scrubber and separator became plugged repeatedly due
to refractory coming oxit of scrubber area,
c) Fibrcclaim is easier to run with the new equipment, but
yield is still unsatisfactory. Laboratory will assist in
determining reason for low yield.
r\
I-:. T. n:
dp
0/30/72
270
-------
fuso U^eoivi.'d, v/^ijlicd
noV wei vjhed -• esti:
Total
Refuse Processed
Process Rate
Fiber Collected anci Sold
Production Race
Fiber Recovered CD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Busis
Cyclone Rejects OD Basis
Water .. '...-'.,.
Organic Materiel OD Basic
Organic Mate-rlrO. Burnpd or Lost
. with Efj:i\.io.')t OD Ba:;is
>?nlpor Operating Time
Reactor Operating Time
Fibreelni.m Operating Time
K lee trie J t y Us od To t a 1
Rate
K£fluonl to MCD
Oil to UohePt Rcr.ctor Total
Rate
ater I7.".od
Rate, Flow
]I;-ILC, per Ton
*BOR
-^ •-- _Tons
_/ /x. ._1
-------
WEEK OP
THRU l/V
Refuse Received, weighed /7? Tons
not woighed-estimated A) Tons
Total /^2l Tons
7 Tons
Refuse Processed
Process Kate
Fiber Collected and Sold
Production Rate
Fiber Recovered
OD Basis
Macaotic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water .
' - • .':"
Oryanic Material OD Basis
Oryanic Material Burned or Lost
.. with Effluent OD Basis
Pulpcr Operating Time-
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used Total
Rate
Eff3uenL to MCD • •
Oil to Reheat Reactor Total
Rate
Water Used
Total
Rate, Flow
Rate, per Ton
*BOR
Tons/hr.
t)ESIGN
267
267
6 ."7
JTors (AD)
_Tons/hr 1. 3
%BOR
20%
Tons
%BOR
19
7%
7-0 Tons
JT, 7 %BOR
3%
Tons
%BOR
D % (Estimated)
%BOR
55
%BOR
Hours
Hours
7 Hours
40_
_4C)_
40
3$OOP KW Hrs.for Plant__41.i2_EL0
KW Hrs/Ton 154
120,000
50 ~~
00"^ Gal Ions
GPM
Gallons
. «/ Gallons/Ton
GPM
Gallon/Ton
K. T.
Based on Refuse
272
-------
;K ot-
THRU
Rcluse Received, weighed
not weigheu-estimatcd
. . . Total
Refuse Processed
Process Rate
Fiber Collected and
Production Rate
Fiber Recovered
OD Basi
Magnetic Metal Recovered OD Basis
nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water . ••• '...-..-, r '
Organic Material OD Basis
Organic Material Burned or Lost
. with Effluent OD Basis
.Pulper Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
Effluent to MCD
Total
Rate
Oil to Roheat Reactor Total
Rate
Water Used
Total
Rate, Flow
Rate, per r
*BOR
_Tons
Tons
Tons
JTons
jTons/hr.
i*»-
Tons (AD)
DESIGN
267
26''
..5 _Ton s
20%
19
%BOR
7%
Tons
7.0 %BOR ,
3%
27
J&BOR 10%
_% (Estimated) 25
55
SI. 7 %BOR
J? / Hours
40
Hours
Hours
40
_KW Hrs.for Plant _4l,
Hrs/Ton 154
120,000
50
Gallons
CPU
Gallons
Gallons/Ton
J
G a 1 lo n
GPM
G a 1 Ion/Ton
Based on Refxise
273 ..
-------
WF.KK OF
__r _ ]jvr)!< Af. ror. AT./FT I'.KKCT.ATM
7/15/7? THRU 7/2 1/72
Refuse Received, weighed
not weighed-estimated
Total
Refuc.e Processed
Process Rate
Fiber Collected and Sold
Production Rate
Fiber Recovered OD Basis
;jc Metal Recovered OD Basis
13 Ton;
203 Tons
Tons/hr
_7C.1~ AD,
Tons/hr
5 %30R*
j.4.8 Tons
7.3 %BOR
6.2 TO,
•js
3•3- %BOR
26.8 To n s
"13"'. 2 %BOR
25.0
50.4 %BQR
45-9 %BOR
28
Hour;
25
Hours
17 Hours
267
267
1.3
20%
19
8
3%
27
10%
25
55
Nonmagnetic Junker Rejects OD Basis
Cyclono Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pulpcr Operating Time
Reactor Operating Time
Fibrcclaim Operating Time
Electricity Used Total'-Since 7/8/72_7J^qop_KW Hrs. for Plant_41-,!52_
Rate 187 K\-f Hrs/Ton 154
35
40
Effluent to MCD — Since 7/8/72
Oil to Reheat Reactor Total
Rate
844,000 Gallons
245 GPM
120,00^.
50
Gallons
2,2 Gallons/Ton
Water Used Total - Since 7/8/72 lf__113,C(X)_Gallon
Rate, Flow . H-L-G™
Rate, per Ton 27j)Ci_GalIon/Ten
*BOR
Based on Refuse
274
-------
r
WJ-:J-;K
Refuse Ki-cr.i vccl ,
S ______ - __ m'! m <\" re rr i\\ ,/'y\ UK rr; .AJ_M
7/H/V2 TJmi, 7/i/j/v,'
not woighed-cntiinaled
Total '
Rof u so I3roce;:Ked
Process Rate-
Fiber Collected and Sold
Production Rate
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Orcjnnic Material OD Basis
Oryanic Material Burned or Lost
with Effluent OD Basis
/
Pulper Operating Time
Reactor Operating Time
Fibrcclaim Operating Time
Electricity Used
Effluent to MCD
Totalj Failed to
Rate / Take
Readings
Oil to Reheat Reactor
Total
Rate
Water Used
Total "\ Failed
Rate, Flow V To Take
Rate, per Tom Readings
_2£L2.
14
Tons
Tons
216 Tons
Tons
DF.SION
267
2£'
1 Tons/hr
L'^;._Tons (AD)
.7 Tons/hr
4.0 %BOR*
18.2 Tons
8 •6 %BOR
20%
19
7%
3 .
Tons
°/oBOR
8
3%
22.. 5 Tons
10. b %BOR
27
10%
25.0 % (Estimated) 25
52.2 %BOR
55
48.2
%BOR
35
30
Hours
40
28
Hours
40
12
Hours
40
_KW Hrs.'for Plant 41, 2:
KW Hrs/Ton 154
_Gallons
GPM
120,000
50
•330 Gallons
1.6 Gallons/Ton
Gallon
GPM
Gallon/Ton
*BOR
Based on Refuse
275
-------
THRU 7/7
Kc£ur.o Received, vciyhou
not weighed-estimatcd
Total
e Processed
Proccr.s Kate
Fiber Collected and Sold
Production Rate?
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Orcjiin.tc Material OD Basis
Oryur.Jc Matoritsl Burned or Lost
with Effluent OD Basis
Pulpcr Operating Time
Reactor Operating Time
Fibredaim Operating Time
Electricity Used Total
Rate
Effluent to MCD
Oil to Reheat Reactor Total
Rate
Water Used
Total
Rate, Flow
Rate, per Ton
*BOR =
7J
Jl'ons
_Tons
JTons
Tons
DESIGN
2G7
2L£__ ._To n s /h r
_/3. Y Tons
7, 9 %BOR
19
7%
6, 1 Tons
J. ±T %BGR
8
3%
Tons
%BOR
27
10%
% (Estimated) 25
%BOR
„$"/ ^ %BOR
*)JL Hours
35
Hours
40
3 . Hours
40
yw Hrs.for Plant 41,250
KW Hrs/Ton 154
Gallons
GPM
120,000
50
Ga lions
Gallons/Ton
_Ga 1 3 en/Ton
Based on Refuse
276
-------
WEK1C 01'' 6/26
THRU 6/30**
Retucc Received, weighed
not weighed-estimated _!]L_
Total
Refuse Processed
Process Kate
FJbrr Collected and Sold
Production Rate
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Waterial OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pulper Operating Time
Reactor Operating Time
Fibrcclaim Operating Time
Electricity Used Total
. Rate
Effluent to MCD
196
Tons
Tons
Tons
206 Tons
6-6 Tons/hr.
Tons (AD)
_0 _ _Ton s/h r
%BOR
15.7 Tons
7.6 %BOR
8.5
Tons
4.1 %BOR
22.3 Tons
10.8 %BOR
52.5 %BOR
31 Hours
23 Hours
Hours
DESIGN
!:67
267
6 . / ' ~
i •?
JL » ,>
20%
19
1%
8
10%
25
25.0 % (Estimated)
52.5 %BOR 55
35
40
40
40
?ft.40Q KW Hrs.for Plant 41, 25
138 KW Hrs/Tori 154
259,340 Gallons
140 GPM
120,000
50
Oil to Reheat Reactor Total
Rate
See next week Gallons
Gallons/Ton
Water Used
Total
Rate, Flow
Rate, per Ton
*BOR
416, OOP XS
230 GPM
2100 Gallon/Ton
= Based on Refuse
277
** = Starting 7/1/72 r.ll weeks will begin on Saturda
-------
TUKU
Refuse Received, v;eighed
not wcighed-cslimated
Total . "
Refuse Processed
Process Rate •
Filler Collected and Sold
Production Rate •
Fiber Recovered OD Basis
Mcujnctic Metal Recovered OD Basis
Nonrvianno.l-.ic Junker Rejects OD Daois
Cyclone Rejects OD Basis
Water ..- •'.<•'.'
Organic Material OD Basis
Orgr.njc? Material Burned or Lost
. -with Effluent OD Basis
P\ilper Operating Time
Reactor Opcreiting Time
210
Tons
12 _ Tons
230 Tons
267
'22'6 Tons
267
6.3 Tons/hr.
0 Tons (AD)
Cors/hr.
0 %BOR--
4.1 Tons
6.2 %BOR
7.9 Tons
8
3.5 %BOR
_2Q .g Tons
9.2 %BOR
3%
27
j.0%
25.0 % (Estimated)
-56.1 %BOR
25
56 . 1
36 . 0 Hours
32.9 Hours
40
iju Operating Time Only for customers Hours
Electricity Used Total
Rate
Affluent to MOD
Oil to Reheat Reactor Total
Rate
•Water Used Total
Kate, Flow
Rate, per Ton
36,000 KW Hrs.for Pliint_4_li,_250.
159 KW Hrs/Ton 154
120,000
267,910 Gallons
125 GPM
50
300 Gallons
JUJ CK- 1 Ions/Ton
470,JGOGa1Ion
2_1J>_ GPM
2030 Gallon/Ton
*BOR
E. T.. Blaklcy/d
Based on •Refuse
278
-------
STATUS
WEEK OF__
y
HYDRAS PO.SAL/FI BRECLAIM
THRU
'•/"- •f-ff
/(."'t^f
Refuse Processed
Fiber Collected and Sol
Piber Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pulper Operating Time
Re-actor Operating Time
Fibreclaim Operating Time
Electricity Used
Effluent to MCD
Oil to Reheat Reactor
Ton
DESIGN
2C7
26
^'BTR*
/
fJor
^Gallons
GPM
Gallons
120,000
50
Based on .Refuse
279
ETB/ip - 6/72/12
-------
STATUS
WEEK OF
HYDRASPOSAL/FT BRECLAIM
6/3 THRU
Qj^l x /
/ """ "*" *•**<>.
Refuse Received
Refuse I'roccL'.scd
Fiber Collcctod and Sold
Fiber. Recovered
OD Basis ,
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone- Rejects OD Basis
Wcitcr
^
Oryr.nic Material OD Basis
Oryanic Matr-rJal Burned or Lost
with Kiflucnt OD Basis
Pumper Operating Time
Reaci-or Operating Time
Fibred aim Operating Time
Electricity Used
" •/
Effluent to MCD
Oil to Reheat Reactor
// /i //
//
-/
* >
tJ
oZ. v5 f Tons
^ » ^ Tons
,'<*,/ Tons
ii * • _
Tons
_2£BOR
Tons
%BOR
_%BOR
Hour:
Hours
Hours
267
19
7%
27
10%
^ (Estimated) 25_
55
40
40
J7 S0^> KW Hrs.for Plant 41, 250
Gallons
GPM
Gallons
120.000
50
*BOR
P.. T. blaklcy/d
ETB/rp-June 14, 1972
_ ,
Based on
280
-------
-STATUS
WEEK OF
THRU
,6c^,X^A£X .
•)+ UJ^I^ (*J%~+*W)
j.'JC Received
Rcfuso processed
Fiber Collected and Sold
Fiber Recover.od OD Basis
Magnetic Metal Recovered OD Basis
i
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Oryan.ic Material OD Bar,is
Organic Material Burned or Lost
with Effluent OD Basis
Pulpcr Operating Time
Reactor Operating Time
Fibrcclaiin Operat.ing Time
Electricity Used
// •
EffJucnt to MCD
Oil to Reheat Reactor
7
Tons
DESIGN
267
/ QTons
„ ;.>iii»
(AD)
%30R*
Tons
19
%BOR
Tons
8
- 1 7 %30R
39L
Tons
27
10%
% (Estimated) 2J5
%BOR
55
%BOR
35
I
Hours
40
Hours
40
2L
Hours
40
^oo KW Hrs.for Plant 41,250
^Gallons
GPM
Gallons
120, OOP
50
Based on KL'fUt!e
E. T. Blakley/d
i of
^281
i-i >:^
%V^5>, 3
****** ±j
:<&
i"T '^VV
-------
STATUS - . HYDRASPO5AL/FIBRECI.AIM
WEEK OF 5/22 THRU 5/28/72
Refuse received, weighed
"liefuse received, not weighed (estimated)
Refuse Received , total
Refuse Processed
process Rote
fc'nbor Collected and Sold
Production Rate
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
-Wal.cr
Organ.ic Material OD Basis
Organ ic Material Burned or Lost
with Effluent OD Basis
Pulpcr Operating Time
Refictor Opereiting Time
Fibreclairn Operating Time
Electricity Used
Electricity Used per ton
Effluent to MCD
Oil to Reheat Reactor
OiJ to Reheat Reactor per ton
Water vised
Water used
Water vs-oed • •
243
?n
263
260
i •
? , 0
0. '
T
Tons
Tons
Tons
Tors /hour
vent, '?:„:,,
Tons/hour
J&DOR*
DBS I OS
267
267
20%
17.2 Tom
6.6
7.8
3.0
29.1
11.2
25
54.2
51.5
36
33
27
43,200
165
19
_%BOR
Tons
8
_%BOR
Tons
%BOR
27
% (Estimated) 25
%BOR
55
%BOR
35
_Hours
Hours
.Hours
40
KW Mrs. for Plant... 41^2.50,
__ KW Hrs./ton 154 _____
Not working Gallons . 120,000 __
--- GPM
340
Gallons
50
240
2,000
1 ,. _3_ gal Ions/ton
' •;/• G a 1 '; '.) n s
GPM
• Gallons/ton
K. T. W
Typed 6/2/V?-Vp
*BOR = Based on defuse
282
-------
^jvyrus_ - HYDRAS ro;.;A!./FT PUKCL* TM
Vil-JKK OF 5/3.5 . THRU 5/21/72
Uofuno received, v;eighed 231 Te*is
Refuoo received, not weighed(estimated) 13
Xffuac Received 244 Tons
J3SSIGN
267
Refuse
Process Unto
fiber Co33ccced and Sold
prodxiction Rate
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
*
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
^
Pulpcr Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
per ton
.23.6
Tons
7.1 Tons/hr
6.5 Tons (AD)
0.3 Tcns/hr
2.8 %BOR*
16 Tons
s
6.8 %BOR
6.8 Tons
2.9 %BOR
23
Tons
9.6 %BOR
52.9 %BOR
33.5 Hours
30
Hours
22
Hours
26 ~
5.3
53
1.3
20°/
19
7%
8
3%
27
25 % (Estimated) 25
55.7 %BOR
55
35
40
40
40
34,200
144
Hrs.for Plant 4.1,250
KW hrs/ton 154 _
Effluent to MCD
Oil to Reheat Reactor
Water used
E. T. Blaklcy/d
Not work ing Ga1Ions
- - GPM
250 Gallons
1^1 Gal/ton
467,000 Gallons
234 GPM
" 1,980 Gal/ton
283
*BOR = Based on Refuse
120,000
50
-------
O'JL t\i UO
J' xr.ixr
WEEK OF 5/8
Refuse received, weighed
Refuse received,not weighed(estimated)
. Refuse Received . •* .. .
f ' ' ' '•
Iicfuf'i; Processed. "
Process Rate
Fiber Collected and Sold
Prod,icLion Rate
Fibn? Recovered OD Basis
V 15xMj,'/etic Metal Recovered OD Basis
THRU 5/14/72
" 241 Tons'
11 TONS
Tons
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water '. . '.-. .
Organic Material OD Basis
Organic Material. Burned or Lost
with Effluent OD Basis
Pulper Operating Tine
Reactor Operating Time
TVibred aim Operating Time
• •* '
Electricity Used - "•
Effluent to MCD
Oil to Reheat Reactor
M ii it
Fresh water used
• n it H - -
.» ii «- - •- • . "-• ' •
\
' J'... T. Blaklcy/d . .
DESIGN
_252
'• ,258
Tons
267
6,25
.0 ?ons- f/D)
____
~2 . 7%30R*
20
|0/
17.3 Tons.
6 . 7%BOR
19
7,9 To.i
3.1%BOR
3%
27.5 Tons
27
. 10.6%DQR
1074
25 % (Estimated) 25
54.6%BOR
55
51.»/oBQR
40
31.3
Hours
22-1 Hours
40
• 37'80G _KW Hrs.for Plant 41,250,
146 KW Hrs./Ton IS^T"
Not working Gallons 120,000. -
GPM 50
210
2'.';
_
-------
STATUS
!!\T)UASPOSAT,/r'Ti3Rv:cy,A.lM
WEEK OF May 1
Refuse received, weighed
Refuse received, .not weighed (est*)
. Refuse Received, total '*
Refuse Processed
Fiber Collected and Sold
Fiber Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pulper Operating Time
Pulper Operating Rate
"Reactor Operating Time
Fibreclaim Operating Time
Fibrcclaim Operating Rate
Electricity Used
Electricity Used KWH/Ton
Effluent to MCD
Oil to Reheat Reactor
?24.8 Tons
15.0 Tons
239.8 Ton s
DESIGN
1 ?.,.. 9 . Tons
6.6- Tons (AD)
3.1
13.8 Tons .
6.5 %BOR
52.4 %BOR
53
20%
19
8
27
6.2 Tons
2.9 %BOR
21,7 Tons
10.1 %BOR
25.0 % (Estimated) 2f>.
55.5 %BOR
55
35
36.5 Hours 40
? 5^8 Tons per hr
'29.0 Hours 40
40
37,800
176
Hours
"TPH
KW Hrs.for Plant 41,2!
154
240
jGallons
. GPM
Gallons
120,000
50
1.1 .Gallons/ton
*BOR
R-
Based on Refuse
285
-------
STATUS
HYDRAS l'OSAL/F I liHSC LA 3. M
WEEK OF
4/24
THRU 4/30/72
Refuse received, weighed
Refuse received, standard fee
Refuse; Received, total
Refuse Processed
Fiber Collected and Sold
Fiber Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with P^rfluent OD Basis
Pulper Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
Effluent to MCD
293
17.
310
Tons
Tons
Tons
DESIGN
207
Tens
..0
17.8
%EOR*
Tons
%BOR
8 . 7
Tons
3.1 %BOR
29.3 Tons
10.5
56,4
%BOR
Hours
39.4
Hours
38.0
Hours
19
8
27
-10%
20.0 % (Estimated) 25
60-0 %BOR 55
35
AO
52,000
Oil to Reheat Reactor
Meter not working Gallons
_ GPM
280 Gallons
KW Hrs.for PI?.nt 41, 250,
120.COO
50
*BOR
Based on Refuse
?86
E. T. Blaklcy/d
iay Ib, llJ>2/rp (the date given to me - rp)
-------
STATUS
HYDKASPOS AVP T F!R K CIAIM
WEEK OF April 17 THRU April 23. 1972
Refuse received, v;eighed 389 Tons
Refuse received, not weighed (estimated) 16 Tons
Refuse Received/ total 405 Tons
Refuse Processed
Fiber Collected and Sold
Fiber Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pulper Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
Effluent to MCD
43'
Tons
G Tons (AD)
2»0%BOR*
,*
25.9 Tons
5.9%BOR-
i
11.3 Tons
2.6 %BOR
40.7 Tons
9.3 %BOR
60.2 %BOR
67 Hours
58
Hours
20** Hours
IGN
.267.
2c?
"1%
8
3%
27
10%
20 % (Estimated) 25
62.2 %BOR
55
35
40
40
40
64,800 KW Hrs.for Plant 41,;
Oil to Reheat Reactor
Meter not work- Gallons . 120,000
. GPM 50
260 Gallons
*BOR
Based on Refuse
287
E. T. Blakley/d
4/25/72-rg
** Fibreclaim downtime due to (1) clean
Hydrasieves, (2) reactor trials, (3) change 2
basket, (4) change thick stock pump -impeller
-------
S
TATUS - HYDRAS PCS AL
WEEK OF April 1C THRU t
Refuse
Refuse
Refuse
received -
received -
Received
weighed
not weighed, estimated
/FIRRECLAIM
^pril 16, 1972
335
13
34ft
Tons
Tons
Tons
DESIGN
267
Refuse Processed
Fiber Collected and Sold
Fiber Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
CycOono Rejects OD Basis
Water
Organic Material OD Basis
Organjc Material Burned or Lost
with Effluent OD Basis
Pulpcr Operating Time
Reactor Operating Time
Fibreclnim Operating Time
Electricity Used
Effluent to MCD
Oil to Reheat Rceictor
.. 6.6 _Tons {AD)
2.1 %BOR*
18.2 Tons
5.8 %BOR
...10.2 Tons
3.3 %BOR
30.3 Tons
9.7 %BOR
59.1 %BC?.
65 Hours
44
Hours
25
Hours
19
8
27
10%
20.0 % (Estimated) 2S_
61.2 %BOR 55
40
40
40
57,600
Meter not workingGaiions
^_ „ GPM
184 Gallons
KW Hrs.for Plant 41,250
120,000
50
*BOR =
K. T. »3cikloy/d
Based on Refuse
288
-------
WEEK OF March 27
THRU April 2, '972
Rcfur.o Received
Rcfuso Processed
Fiber Collected and Sold
F.ibc.-r Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junfcer Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
PuJpor Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
Effluent to MCD
Oil to Reheat Reactor
166
Tons
DESIGN
26
165
Tons
267
7.7 Tons (AD)
4.7 %30R*
13.1 Tons
20%
19
7.9 %BOR
5.6 Tons
3.3
3%
20.0 Tons
12 . 0 %BOR
27
10%
25.0 % (Estimated) 25
55
.1 %BOR
40
23
Hours
40
20
Hours
40
34,200
KW Hrs.for Plant 41,25
4 3Qfoon Ga1Ions
210 GPM
120,000
^460
Gallons
50
*BOR
E. T. BlaXlcy/d
April /i, 1972
Based QjftJig|use
289
-------
STATUS
HYDRAS PQSAL/FI BRECIjAIM
WEEK OF 3/20/72
THRU 3/26/72
Refuse Received **
Refuse Processed
Fiber Collected and Sold
Fiber Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Mate-rial Burned or Lost
with Effluent OD Basis
Pulpcr Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
Effluent to MCD
Oil to Reheat Reactor /
211 Tons
DESIGN
267
2.11
3 (AD)
17.2 Tons
8.1 %BOR
8.4 Tons
3.9 %BOR
27.1 Tons
12.8 %BOR
44.9 %BOR
40 Hours
31
Hours
20
Hours
19
8
27
10%
25.0 % (Estimated) 25^
49.9 %BOR 55
40
40
r
37,800 KW Hrs.for Plant 43,250
653.000 Gallons 120,000
230
jGa lions
. GPM
Gaij-ons
50
E. T.
*BOR = Based on Refuse
** = includes 36.1 torn from Industrial Waste
Disposal on a trial basis.
290
March 27, 1972
-------
STATUS
HYDRAS PCS AL/FI1'^CCLATM
WEEK OF 3/-M/79
THRU
3/10/7 -
Received
Refuse Processed
Fiber Collected and Sold
Fiber Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects. OD Basis
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pulpcr Operating Time
Reactor Operating Time
"ibrcclaim Operating" Time
Electricity Used
Effluent to MCD
Oil to Reheat Reactor
176
"jons
DESIGN
267
170 -,-ons
8.3 Tens (AD)
5..0 %BOR*
12,2 Tons
7.2 %BOR
5.6 Tons
3.3 %BOR
25.0 Tons
14.7 %BOR
44.8 %BOR
35 Hours
.27 Hours
17 Hours
267
53
20%
19"
8
1036
25 % (Estimated) 25
49.8 %BOR
55
35
40
40
43.000 KW Hrs.for Plant 41,250
120.000
300.000 Gallons
145 GPM
Gallons
50
E. T. Blaklo'y/d/rp
March 21, 1972
*BOR
Based on Refuse
291
-------
STATUS
I IYD?.ASr OS AT, /FI PRF, C L A1M
WEEK OF 3/6/72 THRU 3/12/72
Rofuoc Received
Refur.c Processed
Fiber Collected and Sold
Fiber Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Organjc Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pulper Operating Time
Reactor Operating Time
Fibrcclaim Operating Time
»
Electricity Used
Effluent to MCD
Oil to Reheat Reactor
150
Tons
DESIGN
267
. _ Ton a (AD)
12 . 1 Tons
8.0 %BOR
3.8 Tons
2.5 %BOR
21.1 Tons
14.0 %BOR
35. C Hours
29,6 Hours
16,6 Hours**
267
2 or.
19
8
27
25_ % (Estimated) 25
50.5 %BOR 55
40
25.200 KH Hrs.for Plant^.4! , 250,
_53.9..39q_Gallons 120,000
~~160 Gallons
50
*BOR
292
Based on ?(<:,£u n c
K. T. Bl«ik3oy/d
** = Time that slurry is going to Fibieclairr. versus
surge chest. Actual equipment oper .-- ir^; time
is about double this figure.
-------
HYDRAS POSAL/FIBRKCLAIM
WEEK OF 2/28/72 THRU
Refuse Received
Refuse Processed
Fi.br r col Ice! cd and Sold
F?,bor Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rcjecta OD Basis
Org-mic Material OD Basis
Onj.mic Material Burned or Lost
with Effluent OD Basis
?u3pcr Operating Time
Reaetor Operating Time
Fibrcclairn Operating Time
Electricity Used
Effluent to MCD
Oil to Reheat Reactor
I'6S Tons
162 Tons
PESIG;
267
1 7 o/p •••-,
JL » / /oi \
13.4 Tons
8,3 %BOR
5.2 Tons
3.2 %BOR
19.1 Tons
11.8%BOR
51.7%BOR
50.0%DOR
**
36.6 Hours
**
36.7 Hours
7.0 Hours
267
20%
•19
7%
8
3%
27
10%
25 % (Estimated) 25
55
35
40
40
40
59,400 KW Hrs.for Plant 41,2
50
534,520 Gallons
120.000
244 GPM
220 Gallons
50
K. T. Blaklcy/d
*BOR - Based on Refuse
** Extra hours for running organic rejects from
previous week back through system included in
this figure.
•293 ' - .
-------
WEEK OF 2/21/72
Timu 2/27/72
Refuse Received
Refuse Processed
Fiber Collected and Sold
Fiber Recovered
OD Das i s
Magnetic Mota.1 Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Organic Material OD Basis
Organic Material Burned or Lost
with EH:luent OD Basis
Pulper Operating Time
Reactor Operating Time
Fibreclain-i Operating Time
Electricity Usca
Effluent to MCD
Oil to Reheat Reactor
J._56.i4 __ Ton s
.Ton s
DESICA'
267
26?
(AD)
2,6 %BOR*
4.?.j5. %
6.6 Tons
3.5
25
57.7 %BOR
33-
Hour:
10
8
Jlours
Hovirs
53
20
19
8
% (Estimated) 25
55
35
40
40
40
Mrs. for Plant_41.250_
500,000 c,-\-.^nc 120,000
50
Gallons
*BOR
Based on Refu
T. Blnklc'
** = Much stockpiled because reactor was down
294
-------
STATUS
HYDRAS P03 AL/FI Br.ECT.M M
WEEK OF 2/14/72
THRU 2/20/72
'Refuse Received
Refu.c»f? Processed
, Fiber Collected and Sold
f
Fiber Recovered
OD Basi:
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pulper Operating Time
Reactor Operating Time
Fibreclairn Operating Time
Electricity Used
Effluent to MCD
Oil to Reheat Reactor
Tons
Tons
Tons (AD)
6.4 c/oBOR*
11.5 Tons
8.2 %BOR
4.0
Tons
2.8 %BOR
17.4
Tons
12.
%BOR
25
51.5 %BOR
45.1** %BOR
30 Ilours
Hours
12
8
Hours
27
(Estimated) 25
35
40
40
40
48,500 KW urs^or Plant 41.250
500,000 Gallons 120,000
275 GPM
Gallons
50
E. T. Blaklcy/d
295
*BOR = Based on Refuse
** = Stockpiled because Reactor was down
-------
STATUS - HYDRAS 1*03 AL/rTRKECLAIM
WEEK OF 2/7
THRU
2/13
Refuse Received
Refuse Processed
Fiber Collected and Sold
Fiber Recovered
OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Puipcr Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
Effluent to Lagoon
Oil used in Reactor
130 Tons
.4.1
3.3 Tons _~ (AD 5
2.3% BOR*
10.3 Tons
••'7,3% BOR
5 . 0 Tons
3.6% BOR
16.6 Tons
11.8% BOR
*
2 5 . 0% (Estimated)
52.3% BOR
50.0% BOR
25.2 Hours
•24.0 Hours
4.1 Hours
30,600 KW Hours for Plant
306,200 Gallons
1,440 Gallons
*BOR = Based on Refuse
7.96
E. T. Blakley/d
-------
STATUS
HYDRAS POSAL/FIBRECLAIM
WKHK OF 1/31/72 THRU
2/V:/72
received
total
164
Refuse processed
Fiber collected and sold
Fiber recovered AD basis
Magnetic metnl recovered OD basis
Water
Organic material OD Basis
\
Orr/an.ic material burned or lost
with effluent OD basis
Pulper operating time
Reactor operating time
Fibroclalm Operating time
Electricity used
151
2.1
1.3%
11.6
7.7%
Nonmagnetic junker rejects OD basis 4.7
3.1%
Cyclone rejects OD basis 14,1
9.3%
25%
54.9%
53.6%
26
25
34,200
Tons
Tom"
Tons
BOR*
Tons
BOR
Tons
BOR -r
Tons
BOR
(estimated)
BOR
BOR
Hours
Hours
Hours
KW hours for plant
*BOR = Based on Refuse
E. T. Blakley
Fcbi-uary 9, 1972
297
-------
WEHK OF 1/24 thru
Refuse received total
Refuse processed ^ ^ •
Fiber collected and sold
Fiber recovered AD basis
Magnetic metal recovered OD basis
/ __
Nonmagnetic junker rejects OD basis
\
Cyclone rejects OD basis
'
Water ' '
Or
-------
• STATUS.
WEEK OF
THRU
Refuse Received +C?*1-
Rcfuse processed
Fiber Collected and Sold
AO
Fiber Recovered ®S Basls
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
- J with Effluent OD Basis
pulper Operating Time .
Reactor Operating Time
Fibrcclaim Operating Time
Electricity Used
'. *f Tons
Tons
Tons (AD)
BOR*
/!.<)
BOR
J9,o f^—
[3,0% BOR
»T_c% (Estimated)
BOR
BOR
Hours
Hours
A» Hours
37 7
-------
• STATUS " ' lIYDi-.ASPOrJAI./FiniU-,CI,AlM
WEEK OF
Refuse Received
Refuse Processed
*
Fiber Collected and Sold . '.
Fiber Recovered OD. Basis :
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Wciter
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pu3pcr Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used ... . . .* .
Tens
l"^'jj^_
Tons
@- Tons (AD)
O % BOR*
BOR
_
/x.f
7..C % BOR
% BOR
% (Estimated)
% BOR
% BOR
" Hours
Hours
KW Hours for Plant
._ KW Hours for Lagoon
*BOR
Based on Refuse
E. T. Blaklev/b
300
-------
'STATUS
WEEK OF
THRU
/;/.
~
Refuse Received
Refuse processed
Fiber Collected and Sold
Fiber Recovered CD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
pulpcr Operating Time
Reactor Operating Time
Fibrcclaim Operating Time
Electricity Used
Ton.
(AD)
BOR
BOR
BOR
BOR
Hours for Plant
*BOR
Based on Refuse
301
E. T. Blaklcy/b
-------
S'-Vj^P-i LA IM
WEEK OF III THRU
.1.
Refuse Received kmy-*^ ' •-•,,••? Tons
Refuse Processed ' L2iv Tons
Fiber Collected and Sold ' /y? Tons (AD)
Fiber Recovered OS- Basis / '% BOR*
' ^ "T^ A* £
Magnetic Metal Recovered OD Basis 77% BOR
Nonmagnetic Junker Rejects OD Basis /.p% BOR
JH?» f 7~& ***$
Cyclone Rejects OD Basis • ^> % BOR
. Water '. . • • . . -^ % (Estimated)
Organic Material OD Basis *' y/,.S"% BOR
Jr^auic Material Burner], or Lost ^,
with Kffluent OD Basis ^l£_% EOR
•
Pulper Operating Time , 3i/i Hours
Reactor Operating Time . - 3vv/ Hours
Fibrcclaim Operating Time ' '••£• j }lours
\ Electricity Used . A^7 ^.yp KW Hours for Plant
*BOR = Based on Refuse
• -• 302
E. T. Blakley/b
-------
Frank] in Plant Operating Report for Montn of December, 19 .-.
1. OPERATING DATA
Tons x-cceived, weighed 731
Tons received, not weighed 18
Total tons received 749 • 1,160
' . .
Fiber recovered, tons A.D. 36.0 223
Ferrous metal recovered, tons net 61 67
*'
Tone to landfill O.D. 110.3 110
Water to M C D
**''*.
Days operated 24 23
Hours operated:
'Hydrapulper 111 184
Reactor 108^ 184
Fibreclaim 48 184
Rate (based on processed refuse): •
f
Hydrapulper 6.5 TPII 6.25 TPH
Reactor ' 131 #/Min.
Fibreclaira 1.25 TPII
303
-------
Jt£^Xl!LrL.rJL^
Page two
2 . S.hF
• a) No accidents or near accidents were reported.
b) I feel the following every-day operating practices are
unsafe:
1. Raising bucket on BobcaL _:>o high and material
falls into cab.
2. Cleaning Gyro-Flote while running.
c) The following equipment needs guards:
• 1. Washer drum :
. 2. Gyro-Flote weight wheels
d) No recorded past planned action or results.
c) Plans for January are:
1. Purchase enclosure for Bobcat - $165
•* .
2. Install guards on washer drum and Gyro-Flote.
3.. Try to find cleaner to clean slippery floors around
. splashing or leaking equipment.
3' HOUSEKEEPING
a) The present cleanliness of the plant may be satisfactory
for an ordinary plant, but this plant is supposed to be
'a showplace and sales tool and is therefore unsatisfactory.
b} In the past few months several of the mess-causing situa-
tions have been alleviated:
. 1. Pulper hood
2. Hydras ieve covers.
3. Sliding door to replace broken conventional door.
4. Remove tire storage from plant to landfill.
304
-------
cixn Plant Operating Report for Month Oa: December, 1971
three
- continued 4
o) Plans for January are:
1.. Remove sand bags from reactor room and add more
shelves for spare oa^c _;.:i3,,
2. Splash guards for Hydrasieves.
3. Fix Hydradensers so they don't blow.
4. Add cover to conveyor 11 IB (Hydradenser to Rietz Pr /
co if Hydradensers blow then Rietz stays clean.
5. Make workers take pride in the appearance of pi . -.
i
4. J2UALTTY .
1 * k
a) Not many tests were run on fiber this month except for
% grease before and after rewash.
b) Logan-Long were able to run rewashed pulp (pulp 'passeu back
through system using all fresh water) without any of the
previous problems encountered. The success of those trials
indicate the need for a clarifier.
c) Aside from the Bauer Cleaners and the Rietz Press, all
other pieces of equipment have given us problems on
capacity. The following changes have helped or hindered
us as indicated.
. 3.) Larger hole in Selectif ier Screen - showed Hydrasieve
to be under capacity.
2) Smaller hole in V.R. V.R. becomes difficult to
operate and under capacity.
d) Future plans include the following:
1. Add showers to Hydrasieves.
2. Add clarifier . •
3. Speed up V.R.
305
-------
rraiij{.ij>n plantr operating Repofir for month of pecentber, 1971
four
a) The production rate* of the pulping portion of the
system is in line with design, however, the reactor
rate io down due to thickening and feeding limitations.
Fibreclaira's rate is far frorr, design due to Several
pieces of equipment in the system.
Dorr-Oliver has ordered a BC AGO feeder to replace
the currently installed feeder. Shipirr-nt scheduled
for February 14.
b) The maintenance problems encountered in the past month
are:
1. Dismantling of Hydradensers for repair. One screw had
the flight length increased 1/2 flight,- and the
basket perforations were changed from .079 to .094.
Preliminary evaluation indicates that these changes
will correct the problem. If confirmed, the other
two barrels will be changed in late January or
early February.
••
/
2. Being able to. keep hammers on pulper rotor.
• •
A change in design, to provide positive locking of
the hammer hold-down nuts is being evaluated.
• Results are encouraging, but wa will not know if
the problem is solved until the end of January.
3. Maintenance costs are high due to 1 and 2 above
plus two maintenance men and low plant income.
c) Power
Total power consumption for the plant for the month
of December was 168,000 KW hours. This is
233 KWH/ton, approximately as planned.
d) Labor
Overtime
Most of the overtime charged in December was due
toi
306
-------
five
OPERATIONS continued
1. Late starts in mornings ? first garbage
comes in from 8:00 to 10:00.
2« Extra hours o^r"* ,.i< •:.-<-, to reactor c;
Pibreclair* ^.ow ^..oca-c,:-.^ rates,
3. Saturday operation.
4. Rewash trials
5. Extra housekeeping
e) Unusual costs aside from overtime this month were
attributed ko •
1. Repair ani equipment to repair Hydradensers.
2. Tackle for pulper due to hanraers coming off.
3. Fuel, oil because of undercapacity of Hydradensers.
4. Extra power because of extra operating hours.
5. Fast tire wear on Bobcat and fork truck.
6. SUHMAKY
1) The performance of Hydrasposal was satisfactory this
month except for the repeated loss of hampers and the
reduced capacity of the Hydradensers . It was discovered
that the Hydradensers perform much better if as much
fresh water as possible is added to the system.
2) It was determined that the bed levsl in the reactor
was raising at a rapid rate. A hopper is being constructed
to b.e used in the removal of bed material.
3) Fibrcclaim needs much thought and work to bring its
performance up to design. A problem in doing the work
necessary is the overtime involved in the additional
hours necessary for operation and finding a market for
what we do produce even though the yield may ba low.
307
E. T. Blokley
rp
-------
STATUS
HYDROS PCS AL/FI DR^CLM M
WEEK OF
12/27 THRU
12/31/71
Refuse received weighed
Rcfuso received weighed & misc
Refuse processed
Fiber collected and sold
Fiber recovered AD basis
Magnetic metal recovered OD basis
Nonmagnetic junker rejects OD basis
Cyclone rejects OD basis
V
Water
Organic material OD basis
Organic material burned or lost
with effluent OD basis
Pulpcr operating time
Reactor Operating time
Fibreclaim operating time
Electricity used
17?
2.1
1.2%
11. 6
6.8%
4.1
2.4%
20.9
• 12.1%
2.5jQ%
53.7%
52.5%
30
31
149,000
Tons
Tons
Tons
Tons (AD)
BOR*
Tons
BOR
Tons
BOR
Tons
BOR
(estimated)
BOR
BOR
Hours
Hours
Hours
KW hours for plant-
since Dec. 6.
* B01X
Based on Refuse
E. T. Blakley
12, 197?.
308
-------
STATUS
WEEK. .OF
12/20
THRU
12/26/71
5.3
3.7%
10.2
7.3%
4.1
2.9%
Refuse received weighed 125
Refuse received weighed & misc 137
Refuse processed • , I>2
Fiber collected and.sold . __
Fiber recovered AD basis —
Magnetic metal recovered OD basis
Nonmagnetic junker rejects OD basis
Cyclone rejects OD basis
i
Watci: _
Organic material OD basis _
Organic material burned or lost
with effluent OD basis __
Pulper operating time . ' _
Reactor operating time __
Fibrcclaim operating time
Electricity used Hot read
15.8
11.2%
25.0%
53.6%
49.9%
24
26
12
Tons
Tons
Tons
Tons (AD;
BOR*
Tons
BOR
Tons
BOR
Tons
BOR
(estimated)
BOR
•
BOR'
Hours
Hours
Hours
KW hours for plant
*B01l
Based on refuse
E. T. Blaklcy
Jannarv 12, 1972
309
rp
-------
STATUS
HYP ft AS y OS Mi/F IERECLMM
WEEK OF
12/13 thru
12/19/71
Rcf\u;o received weighed
Refuse received misc & weighed
Refuse; processed
Fiber collected and sold
Fiber recovered AD basis
Magnetic metal recovered OD basis
Nonmagnetic junker rejects OD basis
Cyclone rejects OD basis
Water
Organic material OD basis
Organic material burned or lost
with effluent OD basis
Pulpcr operating time
Reactor operating time
Fibrcclaira operating time
EJ.ectricity used
.B4
18!
12.8
6.8%
11.6
6.3%
5.8
18.7
10.1%
25.0%
55.6%
48.8%
36
31
22
Not read
Tons
Tone
Tons
Tons (AD)
BOR*
Tons
BOR
Tons
BOR
Tons
BOR
(estimated)
BOR
•
BOR
Hours
Hours
Hours
KW hours for .plant
*DOR
Based on refuse
E. T. Blakley
January 12, 1972
310
rp
-------
WEEK OF
12/6
THRU
12/12/71
Refuse received
Refuse processed
Fiber collected and sold
Fiber recovered OD basis
I4agnetic metal recovered OD basis
Nonm
agrietic junker rejects OD basis
Cyclone rejects OD basis
YJatcr
Organic material OD basis
Organic material burned or lost
with effluent OD basis
Pulpcr operating time
Reactor operating time
Fib):oc.laim operating time
Electricity used
o
181
5.5%
10.5
7.4%
4.5
3.2%
17.8
12.5%
25.0%
51.9%
46.4%
31
27
21
Not read
Tons
Tons
Tons _(AD)
BOR*
Tons
BOR
Tons
BOR
Tons
BOR
(estimated)
BOR
BOR
. Hours
Hours
Hours
KW hours for plant
* - * BOR
Based on refuse
E. T.
January 12, 1072_
311
-------
STATUS
HYDRAS POS AL/FIBRECIAIM
. WEEK OF
11/15
THRU
11/21/71
•it • •'
Refuse received
Refuse processed
Fiber collected and sold
Fiber recovered OD basis
Magnetic metal recovered OD basis
o
Noniriagnetic junker rejects OD basis_
Cyclone rejects OD basis
Water . .
Organic material OD basis . _
Organic material burned or lost
with effluent OD basis
173
. 16"? -
10.3
5.6%
6.5%
Tons
Tons
Tons
BOR*
BOR
Pulper operating time
Reactor operating time
Fibreclaim operating time
Electricity used
3,5%
12.8%
25.0%
52.2%
(AD)
BOR
BOR
(estimated)
BOR
36
34,300
45.7% V. BOR .
Hours
Hours
Hours
•
KW hours for plant
31
30
*BOR
Based on refuse
E. T. Blakley
December 8, 1971
rp
312
-------
swi'i/s - I-IYDUAS rcs/M./Fipro.-'.c:! .AIM
WIWK OF 11/22 THRU 11/20/71
Refuse roccivc-d
Ro£use processed
Fiber collected and sold
Fiber recovered OD basis
Magnetic metal recovered OD basis
Nonmagnetic junker rejects OD basis
Cyclone rejects OD basis
Water
Organic material OD basis
Organic material burned or lost
with effluent OD basis
Pulpcr operating time
Reactor operating time
Fibrcclaim operating time
Electricity used
132
_«2_
3.0%
;;7.4%
3.0%
' 11.7%
25.0%
52.9%
49.9%
28
27
10
Tons
Tons
Tons (A*. ,
BOR
BOR
BOR
BOR
(estimated)
BOR
BOR
Hours
Hours
Hours
45.000
KW hours for plant
*BOR
Based on refuse
E. T. Blakley
December 8, 1971
rp
313
-------
STATUS
HYDRASPOSAL/FIBRECLMH
WEEK OF
11/15 THRU
11/21/71
Refuse received
Refuse processed
Fiber collected and sold
Fiber recovered OD basis
Magnetic metal recovered OD basis
Nonmagnetic junker rejects OD basis
Cyclone rejects OD basil
Water
Organic material OD basis
Organic material burned or lost
with effluent OD basis
Pulper operating time
Reactor operating time
Pibreclaim operating time
Electricity used
173
167
10.3
5 .6%
6.5%
i 3.5%
12.8%
25.0%
52.2%
45.7%
Tons
Tons
Tons (AD)
BOR*
BOR
BOR
BOR
(estimated)
BOR
BOR
3S
30
.34,300
Hours
Hours
Hours
KW hours for plant
*BOR = Based on refuse
E. T. Blakley
December 8, 1971
rp
314
-------
To Mr. C. C. Landegger/f""" Paul G. Marsh Da{° December 6, 137
BC/NiC i
Coploj To P. A, Alevra, Peter Seifert, W. Herbert
Subject Franklin Plant - Additional File R*f« Franklin Plant
Yield Information: Item No. 3 -
CCL 71-1258 c.r. VR Classifiner
Data collected during the week of Noverroer 2'j to December '->
indicate yields at Franklin in the range of 10 - 15$, using
the Laboratory VR Classifiner.
Tests arc being made in the Middletown Laboratory to relate
yield to the amount of paper fiber present in the refuse.
The relationship between final yield and the amount of paper
present in the refuse will be reported by Peter Seifert.
315
-------
STATUS - HYDRAS FOB AL/^F 1ERECLA ][!•!
V7KLK OF 11/0 TH.ULL 1 11/14/71
Refuse received
Refuse processed
Fiber collected and sold
Fiber recovered OD basis
Magnetic metal recovered OD basis
Nonmagnetic junker rejects OD basis
Cyclone rejects OD basis
Water
Organic material OD basis
Organic material burned or lost
with effluent OD basis
Pulper operating time
Reactor operating time
Fibreclaim operating time
Electricity used
.g;
11.4
6.5
6.9 %
3.5
11.4 %
25.0 %
53.2
46.7 %
28.2
29.2
23.4
34.200
Tons
Tons
Tons (AD)
BOR*
BOR
BOR
BOR
(estimated)
BOR
BOR
Hours
Hours
Hours
KW hours for plant
* BOR
Based on Refuse
E. T. Blakley/rp
November 18, 1971
316
-------
STAl'UG
OF
11/1
;'HRU
ll/ 7/71
Organic material burned or lost
with effluent OD basis'
Refuse received 219
Refuse proccs-sed _____ll2_
Fiber collected and sold ^...^-.l,.
Fiber recovered OD basis __
Magnetic metal recovered OD basis __
Nonmagnetic junker rejects OD basis __
Cyclone rejects OD basis __
Water __
Organic material OD basis _
.4 %
7.1 %
3.7 %
12.5
25.0 %
51.7 %
51.3 %
36.9
42.9
Pulpcr operating time __
Reactor operating time _
Fi'breclaim operating time
Electricity used 46,800
5.0
Tons
•rons
Tons (AD)
BOR*
BOR
BOR
BOR
(estimated)
BOR
BOR
Hours
Hours
Hours
•
KW hours for plant.
%
KW hours for lagoo
o
*BOR = Based 'on refuse
E. T. Blakley/rp
November 9,...197_1
317
-------
STATUS
WEEK OF
10/25 THRU
10/31/71
Refvisc received
Refuse processed
Fiber collected and sold
Fiber recovered OD basis
Magnetic metal recovered OD basis
Nonmagnetic junker rejects OD basis
Cyclone rejects OD basis
Water
Organic material OD basis
Organic material burned or lost
with effluent OD basis
Pulpcr operating time
Reactor operating time
Fibrcclaim operating time
Electricity used
231
7.9
1.6 %
10. G %
.25.0 %
54.7 %
54.7
36
36
Tons
Tons
_C Tor.a (AD)
0 % BOR*
41,400
BOR
BOR**
BOR
(estimated)
BOR
BOR
Hours
Hours
• *
KW hours for plant
*BOR = Based on refuse
= This figure seeiuu Lo i>e in error. Operator must
have failed to weigh several hoppers.
E. T. Blakley/rp
Noycr.-xber 4 , 1971
318
-------
STATUS
HYDR/VSPOSAL/FIBKECLATM
WEEK OF
10/10
THRU
10/23/71
Refuse received
'w
Refuse processed
Fiber collected and sold
Fiber recovered OD basis
Magnetic metal recovered OD basis
Nonmagnetic Junker rejects OD basi:
Cyclone rejects OD basis
Water
Organic material OD basis
Orgnnic material burned or lost
with effluent OD basis
Pulper operating time
Reactor operating time
Fibreclaim operating time
Electricity used
217
Tons
Tens
Tons (AD)
% BOR*
7.4 % BOR
2.9% BOR
11.4 % BOR
25.0 % (estimated)
53.3 % BOR
53.3 % BOR
30
37
34.300
Hours
Hours
Hours
KW Hours for plant
Cannot read KW Hours for lagoc
* BOR = Based on refuse
E. T. Blakley/rp
Octobcr 25, 1971
319
-------
STATUS
WEEK OF
HYDRAS POSftL /F I BRECLAIM
THRU ____ 10/17/71
Refuse received
Refuse processed
Fiber collected and sold
Fiber recovered OD basis
218 Tons
218 Tons
.-.._p Tons (AD)
0 % BOR*
Magnetic metal recovered OD basis 11.2% BOR
Nonmagnetic Junker rejects OD basis 3.4% BOR
Cyclone rejects OD basis 12.2% BOR
Water . 25.0% (estimated)
Organic material OD basis 48.2% BOR
Organic material burned or lost
with effluent OD basis 48.2% BOR
Pulper operating time
Reactor operating time
Fibrcclaim operating time
Electricity used
37.2 Hours
37.6 Hours
0
186,000
Hours
KW hours for plant
since 9/20/71
KW hours for lagoon
*BOR = Based on refuse
E. T. Blakley/rp
October 25, 1971
320
-------
STATUS
WL'EK OF
Refuse received
Re-fuse processed
Fiber collected and sold
j; HYDRAS POS A-L/F I.BREC LA1M
10/4 TliRU 10/1C/71.
Fiber recovered
OD Basis
Magnetic metal recovered OD Basis
Nonmagnetic Junker rejects OD Basis
Cyc-lone rejects OD Basie
Water
Or g an i c rna te r i i\ 1
OD Basis
Organic Material burned cr lost
with effluent OD Basis
Pulper Operating Time
Reactor Operating Time
Fibred aim Operating Time
Electricity used
222
25'
25.0%
61.4%
61.4/0
47.6
60.8
Tons
J 0 Tc*- s
0% BCR*
6.0%** BOP.
1.8%** BOR
5.8%** BOR
(AD)
(estimated)
BOR
BOR
Hours
Hours
Hours
not read KW hours for plant
not read KW hours for lagoon
F.. T. Blakley/rp
October 25, 1971
*BOR = Based on refuse
** = Apparently all hoppers were
not weighed due to new
personnel and St. Regis
sampling.
321
-------
STATUS _^ HYDRASPOSAL/F1BRECLAIM
WEEK OF SEPTEMBER 27, 1971 THRU OCTOBER 3, 1971
Refuse Received
Refuse Processed
Fiber Collected for St. Regis Trials
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone: Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pulporr Operating Time
Reactor Operating Time
Fihroc] ;ri.in Operating Time
Electricity Used
325 Tons
320 Tons
(AD,
3v6% 30?;*
5.6% BOR
3.9% BOR
7.4% BOR
25.0% (Estimated)
58.1% BOR
54.5% BOR
46.9 Hours
46.3 Hours
40.8 Hours
Not Read KW Hours for Plant
Not Read KW Hours for Lagoon
*BOR
Based on Refuse
£ ,(j. &
E. T. Hlakley/b
October 11, 1971
322
-------
STATUS
WEEK OF
TI1R° SEi?
26'
Refuse Received
Refuse Processed
Fiber Collected for St. Regis Trials
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Wai.or
Organic Material OD Basis ^
Organic Material Burned or Lost
with Effluent OD Basis
pulpcr Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
27 £ ^'"ns
241 Tons
15 Tons (AD)
6.2% BOR*
6.5% BOR
3.5% BOR
7.1% BOR
25.0% (Estimated)
57.9% BOR
51.7% BOR
36.4 Hours
.37.6 Hours
31.0 Hours
Not Read KW Hours for Plant
Not Read KW Hours for Lagoon
*BOR
Based on Refuse
E. T. »lakley/b
October 11, 1971
323
-------
/W. Herbert t From Paul G. Marsh Doto September 21, IT 71
W
,io& To C. C. Landegger, P. A. Alevra, R. F. Vokes, E. T. Blakley, P. Seifort,
W. p. Sibcrt
joct Franklin Plant Operation: Rl« Rof. Franklin Plant Operation/
Week of September 13 to . Status (Progress Report)
v September 19, 1971
c.r. Franklin Plant >
The summary for the week of September 13 tr, September 19,
1971 is attached.
We planned to start sampling 40 tons of fiber for St. Regis
Paper Company on September 15. However, we burned two
motors in the Plant on September 15 and had to stockpile
refuse. We started processing refuse again on September 16
Due to a delay in delivery of the packaging materials for
the recovered Fourth Forest Pulp, we stockpiled pulp. This
will be packaged the week of September 20 to 24 , under the
supervision of Mr. D. E. Chupka. We expect our first ship-
merit of Fourth Forest Pulp to be sent to St. Regis on the
23rd of September.
JM
* V^ -•. ^ •" , '**^j
JA S'"\UK. ,'9
x\ s*** y'
PGM/erb
»
Summary - Week of September 13 Tnru September 19, 1971
324
-------
STATUS
HYDRAS POSAL/FIBRECLAIM
WEEK OF SEPTEMBER 13 THRU SEPTEMBER 19, 1971
..*
Refuse Received
Refuse Processed
Fiber Collected for St. Regis Sample
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclono Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
with Effluent OD Basis
Pu]per Operating Time
Reactor Operating Time
Fibrec.laim Operating Time
Electricity Used
2*3 Ions
•*"*, • f .;- f-
'i irons (
3.4% BOR*
6.0% BOR
2.4% BOR
9.5% BOR
25.0% (Estimated)
57.1% BOR
53.7% BOR
32 Hours
32 Hours
20 Hours
36,000 KW Hours for Plant
7,400 KW Hours for Lagoon
*BOR
Based on Refuse
E. T. Blakley/erb
September 22, 1971
325
-------
w,. Herbert
From Paul G. Marsh
faeptemoer
C. C. Landcgger, P. A. Alevra, R. F. Vokes, E. T. Blakley, P. Seifert
W. P. Sibert
Franklin Plant Operation:
WccH of September 6 to
September 3.2, 1971
Fiie R«f. Franklin Plant Operation •'
Status (Progress Report)
c.r. Franklin Plant
The summary for the week of
1.971 is attached.
September 12,
The latter part of the week we operated the Middletown
Pilot Plant on Franklin fiber.
W. IlF-rbert and I visited Logan-Long on Thursday, the 9th
of September. We summarized the information contained
on Table I (attached). This shows that the Fibreclaim
pulp is between 4% and 5% solvent extractables ("grease")
It alr.o shows that Nalco Chemical Petrolite and caustic
soda have little effect on grease reduction. Enzyme
treatment of Franklin pulp had no effect whatsoever. The
most effective treatment for grease remova], was, as previous
data has shown, reverse cleaning. This reduced grease
content from 5.2% down to 3.3%.
.»•
In our conversations with Don Brown, it appeared that he
was not particularly convinced that grease was the problem
in the plugging of his felts. He emphasized that his
yupp.lior had given him a different felt v.'eave and that on
previous occasions he has had problems when the weave of
his felts was changed. Brpwn said that he would be ready
to receive fiber again in about a week. However, we asKed
to postpone delivery since St. Regis will be taking all of
our fiber during the month of Septer-iber. Don said this was
perfectly all right and that he would take fiber again on
a test basis after we have taker our St. Regis samples.
PGM/orb
Enc.
Summary
Table I
Week of September 6 to September 12, 1971^
- Tests on Fourth Forest Pulp and Logan-. Vs-v
Long Fiber
e
o L r
326
-------
STATU S - HYDRASPOGftL/FI &RECUVIM_
WB)-:i; OF SEPTEMBER 6 THRU SEPTEMBER 12, ]CJ71
Refuse Received
Refuse Processed
Fiber Collected and Sold
Fiber Recovered OD Basis
Maynotic Metal Recovered OD Basis
Nonmagnetic Junker Rejects OD Basis
Cyclone Rejects OD Basis
Water
. ; >
Organic Material OD Basis
Organic Material Burned or Lost
' with Effluent OD Basis
Pulpcr Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
0
0%
6.5%
2.8%
9.0%
25%
56.7%
56.7%
32.8
37.7
3.0
37,800
8,300
Tons
BOR*
BOR
BOR
DOR
(Estimated)
BOR
BOR
Hours
Hours
Hours
KW Hours fo
KW Hours fo
*BOR
Based on Refuse
E. T. Blaklcy/b
Scpteiabcr 13, 1971
327
-------
M
CO
M
O
55
s
I
s
H
a
£-1
10
O
(M
o
(M
53
O
CM
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U
W
^
ra
g
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s
B
w
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W
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t
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r
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q Franklin Pulp
c
._J
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r c
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rom 8/30/71
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£
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'71 Pulp
at 20% Consistency
.)
»*• 3% Consistency
1 Consistency
si - 8/30/71 Pulp
1 -x - -.
•f o *O ft T5 in PJ
• • -- •
us tries
Blank
1/100 Enzyme
i /i nn Enzvme
^ 13
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-------
w
Copies To
Subject
'. Herbert
From Paul G. Marsh
Septe.Ttecr 7, li
C. C. Landegger, P. A. Alevra, R. F. Yokes, E. T. Blaklcy, P. Scifo:
W. P. Sibort
Franklin Plant Operation:
Week o£ August 30 Thru
September 5, 1971
File Rel. Franklin Plant Opc-ation/
Status (Progrci L; Rjpor
• c.r. Fr nklin,. Ohio
Attached is the work summary for the week - Augus-c 30 t.vro
Septen\ber 5, 1971.
This was far from a normal week:
1. Logan-Long asked us not to deliver any more pulp
for at least a week to give their, a chance to test
the effect of felt life and board quality. (See
attached memorandum.)
2. The Hydrapulper rotor drive shaft was bent on
September 2 and had to be replaced. This caused
us to shut doxvii during the latter ptart of the
week and over the weekend.
PGM/erb
Enc.
Status - Hydrasposal/Fibreclaim
Week of August 30 Thru September 5, 1971
Memo to the Files - 9/7/7.1 - Logan-Long
c
329
-------
The Files
Paul G. Marsh
Dote
September 7, 197
»
C. C. Landegger, P. A. Alevra, R. F. Vokes, W. Herbert, E. T. Bl£>:lev
P.Scifert, W. p. Sibcrt
Possible Fourth Forest Pulp Rio Rof. Logan-Long Co./Franklin
Handling Problems at Logan-Long
c.r. Fiber Recovery - Handling
During telephone conversation on Auc-cut 20, 1971, I learr.ec'
from Don Brown that he was having probler.s which he believes
are attributable to our Fourth Forest Pulp.
He told me that his felts were filling with a waxy material
and that his felt life had been cut from 30 days to 15 days.
lie is also experiencing a problem with the dry felt cracking
which correlates with the addition of our pulp. In order to
conclusively ascertain that our pulp is in fact the problem,
Don told me that he would not take any more of our pulp for
one or two weeks.
On August 31, Bill Herbert and I visited Logen-Long to discuss
tho problem further with Don Brown. Logan-Long's converters
have 8" rolls. The short radius causes some chocking with
normal furnish. The normal furnish is
10% Corrugated
14% News
16% Mixed Paper
60% Wood
When our material was substituted for the straight blend of
waste paper, more severe cracking problems were noted.
We aslrcd about showers used on the paper machine felts. Don
Brown told us that they had one fresh water shower and one
white water shower on the paper machine felt.
Don Brown emphasized that he wants to work with us on solving
the problem if there proves to be a problem.
*\
Felt Filling
Wo stated that grease may be the cause of felt filling.
Grease content of Logan-Long pulp was .8% (February 19, 1971).
With our pulp added, one test showed 1.4% grease. Based on a
10" addition of Fourth Forest Pulp having a 4" - 5% grease
content, the increase from . 3£ to 1.4S is explainable.
We propose that if grease is the problem, we would attack it at
our plant. There is also the possibility of adding needle
showers and/or chemical on the paper machine at Logan-Long.
330
-------
The Files
Tag- 2 - September 7, 1971
Possible Fourth Forest Pulp
Ikmdling Problems at Logan-Long
Cracking of the Dry Felt ,
Grease removal may help crackinv,, rlcv , s i-. a change :
the \vaste paper blend formula IL. ^ more li/- :-ly solvcic
For iijntance, our pulp might be used ro replace news
instead of the full waste paper mix.
PGM/erb
331
-------
STATUS
HYDRASPOSAL/FIDRZCLAIM
'WEEK OF AUGUST 3C THRU SEPTEMBER 5, 1971
Refuse Received
Refuse Processed
Fiber Collected and Sold
Tiber Recovered - OD Basis
Magnetic Metal Recovered - OD Basis
Nonmagnetic Junker Rejects OD Basis
c
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Malcrial Burned or Lost
with Effluent OD Basis
•»*-
Pulpor Operating Tame
Reactor Operating Time
I'ibrcclaim Operating Time
Electricity Used
222 Tons
175 Tons
.8 Tons (AD)
.5% BOR*
7.2% BOR
3.7% BOR
12.4% BOR
25% (Estimated)
51.7% BOR
51.2% BOR
29 Hours
32 Hours
*
7 Hours
36,000 KW Hours for Plant
7,400 KW Hours for Lagoon
Based on Refuse
07 /
Earl T. Blakley/b
September 7, 1971
332
-------
C. C.
From
11. F. Yokes
September 7, 1 9',
Subject
Copies To ( W. Herbert
Franklin Plant Status
Rio Rof.Soiid Waste Process ing/Ti .:r,'
X Plant
HYDRAPUI/PER DRIVE DAMAGE -- -~ Ci. .... .v -•
picce of steel large enough to ber.u .l^e Hycr^. valv:_-.
shut down. Repairs have been complete c. ..^.. ,
Corrections may include:
a) closer Rurvcillancc of trash
b) shaft diameter and metallurgy modification
c) other (? )
Frankly, I am surprised that we did not have this happen much sooner,
Certainly, the experience will prove to be very valuable.
GREASE REMOVAL -- LOGAN-LONG ---- All chemical methods
have proved to be fruitless.
Reverse centrifugal cleaning removes approximately 50% -- perhapr-
cnough fo] Logan-Long's requirements. Logan-Long meeting scheduled
considering installation reverse cleaners Franklin plant.
We will keep you informed.
RFVokes/fmw
-------
Paul G. Marsh
Ps.om Earl T. Blaklcy
t To <-• c- Lcuidoggor , R. F
Subject Franklin Plant Operation:
Week of August 23 Thru
August 29, 1971
Oat* September 1, 19".
Ji Herbert, P. Seifert, W. P. Sibert
Rio Rof. Franklin Plant Operation/
Status (Progress Report)
• franklin, Ohio
Attached is the summary for the v/eek of
August 23 through August 29, 1971.
Two-shift operation was used August 23
through August 27, 1971 because an
abnormal amount of refuse was brought in
from Dayton by Southern Ohio Sanitation.
or
ETB/erb
Enc.
Status - Hydrasposal/Fibreclaim
Week of August 23 Thru August 29, 1971
334
-------
STATUS
HYDRASPOSAL/FIBRECLAIM
WEEK OF AUGUST 23 THRU AUGUST 29, 1971
Refuse Received
Refuse Processed "•
<,
Fiber Collected and Sold
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Junker Reject OD Basis
•
Cyclone Rejects OD Basis
Water
Organic Material" OD Basis
Organic Material Burned or Lost
in Effluent OD Basis
Pulper Operating Hours
Reactor Operating Hours
Fibreclaim Operating Hours
Electricity Used
291 T^ns
2>— 'i=o~iS
17.6 Tons (AD5
5.6% BOR*
8.1% BOR
3.8% BOR
13.4% BOR
25% (Estimated)
49.7% BOR
44.1% BOR
47
47
29
52,200. KW Hours 'for Plant
5,600 KW Hours for Lagoon
*BOR
Based on Refuse
ETB/erb
335
-------
W. Herbert.
From E. T. Blaklay
August 26,
Copiot To K- F- Vokes (2), p. G. Marsh, P. Seifert, W. P. Sibert
Subjoct Fr;mklin Plant Operation:
Wcn-k of August 16 Thru
Amjusl 22, 1971
File Rof. Franklin Plant Operation/
Status (Progress
c.r. Franklin Plant
Attached is the summary for the week of
August 16 through August 22, 1971.
Due to large tonnage of refuse received
(especially August 17, 1971 - 95 tons),
two-shift operation was started on
August 18, 1971 and continued through
August 20, 1971.
ETB/erb
Enc.
Status - Hydrasposal/Fibreclaim
Week of August 16 thru August 22, '1971
336
RECEIVED'"'
AUG 2G 1971
BL/CK'CLAY/20*!
-------
STATUS
JIYDIIASPOSAL/FI B RECLAIM
V7KEK OF
UCUJ^T _22 , 1S71
Refuse Received
Refuse Processed
Fiber Collected and Sold
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Material OD Basis
Cyclone Rejects OD Basis
Water
Organic Material OD Basis
Organic Material Burned or Lost
in Effluent OD Basis
Pulper Operating Time
Reactor Operating Time
Fibreclaim Operating Time
Electricity Used
275 Tons
o
275 r"ohs
18.5 T^.is (AD)
6.2% BOR*
7.3% BOR
5.1% BOR
11.8% BOR
25% BOR
50.8% BOR
44.6% BOR
44 Hours
41 Hours
33 Hours
39,600 KW Hours for Plant
•5,120 ** KW Hours for Lagoon
*BOR
Based on Refuse
**Low because aerator was unknowingly shut down for
three days due to power failure.
ETO/erb
August 26, 1971
337
-------
STATUS - HYPRASPOSflL/FIBRECLMM
WEEK OF AUGUST 9 THRU AUGUST 15, 1971
Refuse Received
Refuse Processed
Tiber Collected and Weighed
Fiber Sold
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Metal OD Basis
Cyclone Rejects OD Basis
Watc:::
Organic Material
Organic Material Burned Or Lost
with Effluent
Pu.lpor Operating Time
Reactor Operating Time
Fibrcc.laim System Operating Time
Electricity Used
215 Tons
215 Tons
16.4 Tons (AD)
16.4 Tons (AD)
6.9% BOR*
7.6% BOR
4.1% BOR
11.4% BOR
v. -' *
25% BOR (estimated)
51.9% BOR
45.0% BOR
31 Hours
28 Hours
27 Hours
37,800 KW Hours for Plant
' 9,360 KW Hours for Lagoon
*BOR
Based on Refuse
C.CT.
«l
KTB/crb
August 19, 1971
338
-------
•P. C. Mar:;h 8/18/71',. fmw
OFFICE MEMORANDUM
FROM:
TO:
CARL C. LA1IDEGGER
Mr. R. F. Voices
KEY/ YOKK, August lO, 19/1
' CCL-71-93G
SUBJECT:
Thank you for sending me a copy of Paul Marsh's weekly report
dated August 5. •
1 . Rega rd i mi. the hau 1 i n£_ c^sts . , r wjw ^ jdon^t^wo s trnol J^pu.t __
wh e el ._ o j tjxe ?wh j c h s jfs _u KJcr_ t je" ' "
Then every day either at the beginning or at the end of
the day, the little truck that we use to push the garbage onto
the conveyor could drag this over to Logan Long.
The entire trip back and forth shouldn't take more than
half an hour. And this system would mean that the transportation
costs would be virtually zero.
2. Inoticea heading of, "Cyclone Rejects 11. 6%. " Is
*• • •,.•.! ,-> * -J-.V^X^>>V ^^>^&A*-^»^«-^ Jrauw'nnfimr.^w**^^* g^ygy^-^M^^y-^sTr j»KX*«^^-J»r «fc»»» *»*•?*• — W«W
this the glass pile?
3 .
Jasls .
a ndjconc.i.s e_LejX)rtj _a_nd I
i^
CCLandegger
339
-------
/W. Herbert From Paul G. Marsh D6t» August 1G, 197:•
^ — ' Dictated 8/13/71
pie» To R. F. Vokcs (2), E. T. Blakley, P. Seifert, W. P. Sibert
bjoct Franklin Plant Operation: file Ref. Franklin Plant Operation/
Week of August 2 - August 1, 1971 Status (Progress Report)
. c,r. Franklin Plant
The summary for the week of August 2 to August 7 is attached.
On August 2, we held Open House for Black Clawson employees.
Due to shutting down to make adjustments, fiber recovery does
not look exciting; however we are making significant progress.
During the week we removed an .062" (hole size) basket and
installed an .079" in the 24P.
We also completed installation of a 1/4" perforated plate in
the Gyro-Flote Screen. This plugged; however compared with
the 1/8", which was replaced, operation improvement was marked.
Correction: Correct July 26 - August 1 Weekly Summary.
Organic content was not the 48% reported but 51.7%.
PGM/erb
Enc.
Status - Hydrasposal/Fibreclaim
Week of August 2 to August 7, 1971
t>
-------
STATUS _- HYPRASPOSAL/FIPRT.CLAI_M
WEEK OF AUGUST 2 TO AUGUST 1, 1971
Refuse Received
•
Refuse processed
Fiber Collected and Weighed
Fiber Sold
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Metal OD Basis
Cyclone Rejects
Water
"""'organic Material
pulper Operating Time
Reactor Operating Time
Fibreclaim System Operating Time
2i,5 i'ons
231 Tons (48 T/D on a 5-day/'.
basis)
10.6 Tons (AD)
10.6 Tons (AD)
4.2% BOR*
7.7% BOR
3.9% BOR
11.4% BOR
25% BOR (estimated)
51.0% BOR
35 Hours
39 Hours
33 Hours
*BOR
Based on Refuse
PGM/erb
August 16, 1971
341
-------
W. Herbert From Paul G. Marsh D«*o Auc-ust 1C, 1971
-W ' . Dictated 6/13/71
:opic$ To R. F. Yokes (2), E. T. Blakley, P. Seifert, W. P. Sibert
ubjocl Franklin Plant Operation: Rio Rof. Franklin Plant Operation/
Week of August 2 - August 7, 1971 Status (Progress Report)
c.r, Franklin Plant
The summary for the week of August 2 to August 7 is attached.
On August 2, we held Open House for Black Clawson employees.
Due to shutting down to make adjustments, fiber recovery does
not look exciting; however we are making significant progress.
During the week we removed an .062" (hole size) basket and
installed an .079" in the 24P.
We also completed installation of a 1/4" perforated plate in
the Gyro-Flote Screen. This plugged; however compared with
the 1/8", which was replaced, operation improvement was marked.
Correction; Correct July 26 - August 1 Weekly Summary.
Organic content was not the 48% reported but 51.7%.
PGM/erb
Enc.
Status - Hydrasposal/Fibreclaim
Week of August 2 to August 7, 1971
342
-------
STATUS - HYDRASPCSAL/riBRKCLiMtl
WEEK OP AUGUST 2 TO AUGUST 7, 1971
Refuse Received
•
Refuse Processed
Fiber Collected and Weighed
Fiber Sold
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Metal OD Basis
Cyclone Rejects
Water
Organic Material
Puiper Operating Time
Reactor Operating Time
Fibreclaim System Operating Time
kvb Tons
231 Tor.s (48 T/D on a S
basis)
10.6 Tons (AD)
10.6 Tons (AD)
4.2% BOR*
7.7% BOR
3.9% BOR
11.4% BOR
25% BOR (estimated)
51.0% BOR
35 Hours
39 Hours
33 Hours
*BOR
Based on Refuse
PGM/erb
August 16, 1971
343
-------
W. Herbert F™m Paul G. Marsh Dcta August 5, 1971
R- F. Vokes (2) , E. T. Blakley, D. H. Kohlhepp
Franklin Solid Waste Plant Rio Rof. Franklin Plant Operation/
Progress: «• Status (Progress Report}
Week of July 26 to August 1, 1971
c.r. Franklin, Ohio Plant
c.r. Logan-Long Co./Franklin
c.r. Cohen Brothers Ir-:.
c.r. Huron Valley Shec•';/<• urtro: ,:
The production statistics for the Franklin Solid Waste Plant
for the week of July 26 to August 1, 1971 are attached.
Hydrasposal System
We are working on several problems in the Hydrasposal area:
X
1. Wear on the Hydrapulper dump purnp - fill in
observation port, build up with weld and ceramic
coat.
2. Insufficient capacity on the airlock feeder to
the Fluid Bed Reactor - Kohlhepp proceeding
with Dorr-Oliver to get a new feeder.
3. Insufficient capacity of the Hydradcnserc -
tighten down discharge plugs, produce thicker
feed stock feed to the Hydradenscrs (3-vane
rotor, more thickening of rejects in the
Fibreclaim System).
4. Bearing problems on submerged bearings (JU Pumps,
agitators) - replace Graphitar bearings with
Delrin plastic.
Fibreclaim System
We were able to run fairly consistently in the Fibreclaim
System. Host of the mechanical bugs are out of the system.
The main cause for shutdown has been problems with dilute
rejects which have interfered with the operation of the
Hydrasposal System.
-------
w. xic'i. jjei. i. •*»
Page 2
August 5, 1971
Fibre-claim System - continued
Some of the problems worked on in the Fibre claim System are
reported below:
1. Yield
In the report of the week of July 19 - 24, 1971,
I stated that the 24-hour rate of the Fibreclain
System was 13.5 tons per day. This has actually
figured out to be 9.7 AD tons per day. Tests
have shown that we are losing fiber mostly from
the fine screening system. We will install a
coarser screen (.079" perforations) in the 24P
Screen (the 12P Screen already has an .079"
perforated basket), and install 1/4" openings on
the Gyro-Flote Screen next vcek. We will also
plan to conduct a thorough c^eck on system
operation just as soon as the larger perforations
are put in service.
2« • Hauling Cost
With open top containers (from Cohen Brothers)
holding 30 to 40 yards and using 15 to 20 pickups
per month, our hauling cost to Logan-Long would
be $700 to $1000 per month. This is based on a
production rate of about 4 tons per day. Our
potential gross earnings on a 4-ton per day basis
are about $2000.
During the week we tried a 30-yard compactor with
the hope that we might compact stock sufficiently
to reduce our transportation cost to a reasonable
level.
Although we did not completely fill the compactor,
it is evident tnat this would not substantially
reduce our hauling cost.
We feel that our best bet is to use a dump truck
and haul the material to Logan-Long with our own
people.'
3. Dilute Rejects^
Wo hope to solve the dilute reject problem early
next week by putting the Gyro-Flote Screen in
service on our rejects. If the screen operates
properly, we should be able to thicken cur rejects
to much higher level. This, is necessary for good
Hydradcnser operation in the Hydrasposal System.
345
-------
Pago 3
Auyutit 5, 1971
Fibrcclaiiri System - continued
4. Nonmagnetic Metal Recovery °
The nonmagnetic residue from the Hydrapulper
should be of greater value than the magnetic
metal providing a way is found to separate
aluminum, copper, brass, etc. We have passed
the nonmagnetic residue back through the
Hydrapulper. This reduced its volume and
weight by one half.
Wilbur Cohen has informed me .that Huron Valley
Steel in Detroit may be interested in this
product. I plan to call Mr. Gib Sequin,
Telephone No. 313/941-3400, to discuss
possibilities of selling him our nonmagnetic
residue.
PGM/orb
Enc.
Status - Hydrasposal/Fibreclaim
Week of July 26 to August 1, 1971
\
346
-------
STATU -
WL'KK 0? JULY 2G TO AUGUST 1, 1971
Refuse Processed
Fiber Collected and Weighed
Fiber Sold
Fiber Recovered OD Basis
Magnetic Metal Recovered OD Basis
Nonmagnetic Metal OD Basis
Cyclone Rejects
Water
Organic Material
J'ulper Operating Time
Reactor Operating Time
Fibreclaim System Operating Time
220 Tons (44 T/D on a 5-day/v:ec}
basis)
S.I/ j/or.s (AD)
8.9 Tons (AD)
3.7% BOR*
7.8% BOR
3.9% BOR
11.6% BOR
25% BOR (estimated)
48.0% BOR
34 Hours
41 Hours
25 Hours
*BOR
Based on Refuse
PGM/erb
August 5, 1971
347
-------
W. Herbert ^9m Paul G. Marsh Date July ^i, iy/j.
*•" '
topics To R. F. Vokes (2), E. T. Blakley, D. H. Kohlhepp
o
Subject Franklin Solid Waste Plant Rle Ref. Franklin Plant Operation/
Progress: Status (Progress Report)
Week of July 19 to July 24, 1971
c.r. Franklin, Ohio Plant
c.r. Logan-Long Co./Franklin
c.r. Cohen Brothers Inc.
c.r. Suburban Sanitary Service
Attached is the production summary for the week of July 19 to
July 24, 1971.
The production rate of the Fibreclaim System is about 13.5 tons
per day (AD basis).
The VR Classifiner bottleneck has been overcome by increasing
rotor speed from 760 RPM up to 1060 R?M. We are consistently
operating the 12P Screen as a reject screen using .079 holes.
We have ordered a 1/4" perforated plate for the Gyro-Flote
Screen so that we can further improve yield.
We have delivered the first fiber to Logan-Long. This was
processed on July 24 by feeding it into their Hydrapulper with
no apparent problems. The bulk of our material has presented
a problem in shipping. A 30-yard container will hold only
4 tons. On July 23, I met with Mr. Wilbur Cohen and made plans
to try a compactor container. Using a compactor, a 30-yard
container should hold 9-10 tons.
I had a visit from Mr. Brooks of Suburban Sanitary Service.
He is interested in our non-magnetic junker rejects. I gave
him a 5-gallon sample of this material and asked him to make us
an offer. Meanwhile Wilbur Cohen has looked at this material
and is interested.
PGM/erb
Enc.
Status - Hydrasposal/Fibreclaim
Week of July 19 to July 24, 1971
348
-------
STATU_S •- _ HYDRASPOSAL/FIBHKCLAIM
WEEK OF JULY 19 TO JULY 24, 3971
Refuse Processed
Fiber Recovered
Fiber Collected and Weighed
Fiber Sold
Macjnetic Metal Recovered OD Basis
Non-Magnetic Metal OD Basis
Cyclone Rejects
Water
Organic Material
Pulpcr Operating Time
Reactor Operating Time
Fibreclaim System Operating Time
213 Tons (43 T/D on a 5-day/wec
basi?)
„,-, , 'Ic.is per Day (2-. -..,,_
8.7 Tens (AD)
4.5 Tons (AD)
7.8% BOR*
3.6% BOR
12.4% BOR
25% BOR (estimated)
51.2% BOR
35 Hours
38 Hours
16.2 Hours
BOR
Based on Refuse
PGM/orb
July 27, 1971
349
-------
RKl'OKT OF MCF.'TINC WJ71I VKN^OR
Company:
Meeting Place
Date:
Subject:
Keport By:
Dorr-Oliver Incorporated
Middletown, Ohio
July 13, 1971
Franklin Solid Waste Plant,
Status_of F/S Disposal Systen
\
Dean H. Kohlhepp
Dorr-Oliver Personnel Present:
R. A. Marti.raucci, Supervising Project Manager
II. W. Richards, Director Process Engineering
David Kellerher, Process Engineer
E. L. Wilson, Construction Supervisor
Black Clawson Personnel:
P. G. Marsh
E. T. Blakley
W. P. Sibert
D. H. Kohlhepp
Copies of Report to:
H. F. Yokes
W. Herbert
P. G. Marsh
W. P. Sibert
E. T. Blakley
Meeting v/ns held at the request of l-'artimucci to dincuss status
of the F/S Disposal System at Franklin.
The v/riter advised that with certain reservations, the Dorr-
Oliver System hac and is performing satisfactori.ly to date. The
reservations cited are:
1) ROTARY VALVE - PNEUMATIC FEEDER SYSTEM EQ. £119
Rotary Valve for the Feeder System supplied for Dorr-
Oliver (D-0) by Allen-Sherir.an-Hoff (A-S-K) must be
replaced by ons that will perform satisfactorily with-
" ' out plugging. The selection of this type and size
valve was made, according to Martimucci, on the basis
of samples and infor^aticn supplied by Black Clawscn,
and especially a bulk density figure of 28j?/cu.ft.
(wet) vs 16?r/cu.ft. as produced currently.
Hovcve.-r, D-0 Suocs. da tod May G, 1970 do not refer -;o
bulk densities buc induce only j.ecd characteristics
as 132;J/~lin 40^ solids, 35% volatile solids 7000
Btu/j; of total solids. 8800 Btu/,;:- volatile solids.
350
-------
REPORT OF MEETING W1VH
1)
ACTION
2)
3)
4)
ROTARY VALVE - PNEUMATIC —/£D
rrsTEM E(
The original A-S-K Valvo began plugging at feed
rates as low as 60^/nin, and we-it chronic at
80 - gOff/ndn at which rate the 3tu rating of
1,000,000 Btu/min for thr: P-jac'-or was reached.
We requested D-O ulc.ic > .-J-H revicv; ou;..
requirements firsthand at Fr~r./:liri and furnisa
the proper valve. Th^s tr. be c j»ne as soon a:-,
possible as the substitute Fic-Tronis Valve wii}
not last.
NOTE: P. Marsh to check on original feed data
supplied to D-O. We are to supply new
data - bulk density wet and dry, lump
characteristics, sizes, etc.
REACTOR COOLING RATE
.30
D-O was advised temperature fall-off on shutdown
is averaging about 15°F/hour instead of the
10°F/hour specified. This results in excessivo
drop of 600°F over a 40-hour weekend cutoff. It
is necessary to bring an operator in Sunday to
step temperature up with auxiliary fuel burners.
D-O suggested prior to shutdown increase bed
temperature to maximum, approx. 1600°F. or until
Scrubber alarm is touched off (limit 200°F.).
They also suggested bed temperature reading would
be low unless bed turned over first. (This is
our standard procedure.)
MAKEUP SAND - REACTOR - EQ. #130
D-O provision for adding makeup sand to the
Reactor through a funnel on the front platform is
clumsy and impractical. We requested recommenda-
tions on a more satisfactory method'." Either by
continuous feed through the Pneumatic Feeder System
or a separate Pneumatic System. To date, after
four weeks plus operation, no sand loss or pressure
differential drop has been indicated.
REACTOR CONTROL PANEL
Temporary Poly-Flo Tubing to freeboard pressure.
Original copper line to be rechecked and put back
into service - by Hughes-Bechtol.
351
-------
T* 7 'i V" T" fM T x T r~ T«'^(1TT
i 1-lt.i.i JL itle.
MarTTmucci clearly stated to me that unless an
acceptable settlement schedule is worked out, D-0
would bo reluctant to spend laore money at this time
on such things as the Rotary Valve problem.
«*
DACKCHARGES
1) -Heat- fpr-- fisacto^-Durlrj^R^^^
Gustav Hirsch submitted a bill for $900.00 plus for
heaters and electricity .^ppliec? curxng construction
period. I have advised hum at the time the bill was
• submitted and today that thi.^ w^s not to Black
Clawson's account. ACTION-, A. M. KINNEY
352
-------
ol
RTJPOKT OF MKET1NG KITH ViiN
BACKCHARGES
continued
2) Fluidizing Air Blower Motor
D-0 backcharge incurred from GE when motor specs
were changed from 400 h?, 1JI" /clt to 500 K?,,
460 volt. Should DG ^o _y-0 . ~o it. Black
Clawson did not initiate tnis change. Ref: Dr:.\
letter to Dorr-Oliver dated Octooer 26, 1970.
3) 90 man-days extra engineering incurred by Dorr-
Oliver in reorienting Scrubber-Separator
configuration to agree with AI-1K Bed Drawings.
Not Black Clawson's responsibility per DHK's
letter to Dorr-Oliver dated October 26, 1970.
DHK/erb
July 15, 1971
V-
353
-------
Av. tierbert
WKBB
From
Paul G. Marsh
Dato July ID, 19 7
>p!ci To R. F. Vokes (2), E. T. Blakley, D. H. Kohlhepp
Franklin Solid Waste Plant
Progress:
Week of July 12 to July 17, 1971
R!e Rof. Franklin Plant Operation/
Status (Progress Report)
c.r. Franklin, Ohio Plant
c.r. Logan-Long Co./Frr- >.li.'>
The production summary for the Franklin Pi^nt for
of July 12 to July 17 is attached.
liS week
We worked on the Fibreclaim System all week. We are pro-
ducing fiber at the rate of 2 - 3 tons/day, but took repeated
shutdowns to improve performance. The feed to the VR
Clascifiner is limited and is presently the bottleneck.
On July 15, we put in a container to catch fiber for trans-
port to Logan-Long. Don Brown, Mill Manager of Logan-Long,
visited the Plant on July 16. He liked the looks of our
fiber and will run it when we deliver a full container.
(About Thursday, July 22) .
PGM/crb
Enc.
Status - Hydrasposal/Fibreclaim
Week of July 12 to July 17, 1971
354
-------
STATUS - HYDRASP03AL
WEEK OF JULY 12 TO JULY IV, 1971
Refu.sc: Processed
Fiber Collected
Magnetic Metal Recovered OD Basis
Non-Magnetic Metal OD Basis
Cyclone Rejects
Water
Organic Material
Pulpcr Operating Time
Reactor Operating Time
{46 T/D on a 5-c
basis)
2000 - 4000 Ibs.*
7.9% BOR **
3.8% BOR
11.1% BOR
25% BOR (estimated)
51.2% BOR
36 Hours
40 Hours
* Estimated (Fiber cannot be weighed until
container is full.)
** BOR
Based on Refuse
PGM/crb
July 19, 1971
355
-------
£\L_ Herbert From Paul G. Marsh Date July 13, 1971
x_,
Dopic! To K. F. Vokcs, D. H. Kohlhepp, E. T. Blaklcy
t>
Franklin Solid Waste Plant Filo Rof. Franklin Plant OpeinUon/
Progrc-ss: Week of July 6 to Status (Progress Kcoort)
July 10, 1971
c.r. Franklin, Ohio Plant
The status summary for the week of July 6 to July 10 is atta hed.
Note that the amount of refuse processed was down by about 10 tons
over the preceding week. However, in general, results are a
duplication of previous weeks.
On July 10, we installed the 7/8" perforated bedplate. The 3/4"
perforated bedplate was badly worn.
The Fibreclaim System has still not operated up to design. The
bottleneck was getting stock to the 24P. The screen supply pump,
an AN Pump, is misapplied. The pump plugged with strings.
Corrective measures taken were to cut out every other vane in the
impeller on the pump and to close up the gaps in the VR Classifincr
bedplate to minimize the passage of strings.
On July 8, we produced 1000 Ibs. of fiber. This was processed
further in the Middletown Pilot Plant on July 9. In general, opera-
tion in the Pilot Plant was encouraging. Problems with low yield
and J ow digester pressure were encountered.
Several samples were sent out during the week. We sent glass
samples to:
Colorado School of Mines 100 Ibs.
Ore Sorters Limited 100 Ibs.
Professor Ward R. Malisch 55 -gallon drum
University of Missouri/Rolla
Analysis of the glass was typically:
-8 Mesh 30%
-3/8" + 1/8 63%
+3/8" . 7%
We are being plagued with numerous problems of a serious nature
(see attached list) . We should meet f oon to decide on courses
of action. Items 5, 6, 9, 17, and 18 require fast action.
*5 c r
PGM/erb
Enc. Status - HYDRASPOSAL/FIBRECLAIM - Week of July 6 to July 10,,
List -- Franklin Solid Waste Plant Problems
-------
STATUS - HYDRASPCSAL/VIDRECLAIM
WEEK OF JULY 6 TO JULY 10, 1971
Refuse Processed
Magnetic Metal Recovered OD Basis
Non-Magnetic Metal OD Basis
Cyclone Rejects
Water
Organic Material
Pulper Operating Time
Reactor Operating Time
'- - -•? ,--^. . . / A "5 ™/n nn -• ?
^. ^~ .' ^W/Jiv-J '^T^X A. / LJ ^-'*i ^* -^
8.1% BOR*
5.0% BOR
10.5% BOR
25% BOR (estimated)
51.4% BOR
34 Hours
37 Hours
*BOR = Based on Refuse
PGM/erb
July 13, 1971
,'K/ WL 14 1971 {-
ci/,r,K avvso;! .r/
357
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FRANKLIN SOLID WASTE PLANT PROBLEMS
•1. . GROUNDS
The Woods appear to be growing batter than the grass.
N. T. Neff says the grounds people, arc not finished.
My recommendations: Get Neff to have landscapers
return to finish work.
2. APPROACH APRON TO TIPPING FLOOR
We use this area for dumping every day. On windy days
refuse will blow.
Recommendations:
a, Erect a Cyclone fence each side of the apron
to catch blowing papers.
b. Extend covered area. The cost of this per
Tom Neff will be about $50,000.
Another problem is that this area is paved v/ith asphalt.
Concrete would have been better.
3. TIPPING FLOOR AND SCALE HOUSE
A. Dust level is high in this area. Dust is getting
in scales, cash register, and calculat9r in scale
house.
Recommendation:
Small air conditioner for scale house.
B. Accumulation of unpulpable debris.
Solution:
Borrow truck from City of Franklin to truck material
to.landfill. - Done July 12.
4. FEED CONVEYOR
Excessive dirt including pieces up to 12" square is carried
over and drops into the conveyor pit. Pit is difficult to
clean.
Recommendation: 353
Catch material in a bin - shorten bottom of conveyor.
-------
PULPER
A. Excessive Wear of Tackle.
Peter Siefert will report 0,1 wear nd make
recommendations. PGM and : ~ -3 : believe
wear on bedplate is exc.c : --'id that
which can be attribu .. • . L ^z . . ~ wear st-rips
which wore lost soon after L .~ :t. , opera tio.-.3.
Recommendation :
Consider cast bedplate out of harder material
or hard overlay.
*•
B. Dust and Splash
i
Pulper vicinity is excessively dirty due to dust
and splashing. This is a very serious problem.
Dust and dirt are damagin our"ti • compressors,
splashing visitors, and wasting i,,unpov7er on
cleanup.
Recommendations :
Install vented hood over pulper. Consider
extending hood back over feed conveyor to the fire
wall to replace fire door.
C. Low Stock Consistency
Extracted stock consistency was too low with 3/4"
holes and four (4) vanes on the rotor.
Recommendations :
a. Go to larger holes - done July 10.
o
b. Go to 3-vane rotor so that pulper can be run
'at higher consistency without overloading the
motor.
JUNKER
The Junk Remover must be cleaned out daily in order to
keep the chain from jumping off the sprocket. Becavise
of small opening on one side, this is time-consuming.
Recommendations :
Lower large dcor and equip with quick opening fasteners
Move small door to opposite side.
359
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FRANKLIN SOLID WASTE PLAKT PROBLEMS Page 3
7. PIPING
ii-«r._Mimr_jv— - f
Much of the piping in the plant vibrates excessively.
* •••
Recommendations:
®
Study and install further bracing.
8. LIQUID CYCLONE
A. Short Cycle Time
Liquid Cyclone cycle is less than two minutes.
We predict high valve maintenance.
Recommendation:
Put larger reject chamber on cyclone - needs
study.
B. Organic Dirt in Rejects and Loss of Heavies to
Sewer
We need a better arrangement for elutriating
cyclone rejects. Perhaps a drag conveyor in a
larger tank.
9• INSUFFICIENT SOLID WASTE SUMP PUMP CAPACITY
The solid waste sump pump is undersized under present
conditions.
Recommendations: .
a. Increase pulper extraction stock consistency. '
b. Speed up pump. Replace 15 HP motor with a
•20 HP.
10. PAINTING *~
The painters have not finished painting the plant.
Tom Neff should be reminded to get this done.
11. REACTOR
A. Call In for Heat-up
In order to keep temperature above the point whore
bed guns can be used (1150°F), we need to have a
man in on Sunday,
-------
FUAKXLIU SOLID WASTE PLANT Pi^OPLJinS Page 4
REACTOR - (continued)
B. Scrubber Overflow
Water overflowing from Fluid Bed f :rubber makes
excessive water which must be r posed of.
Solution:
Replace broken Rotometers for better control of
flow to scrubber.
C. Sand Makeup
We need an approved plan from Dorr-Oliver for
method of adding sand to the bed.
12. DOOR IN METAL SORTING AREA
Doors arc small and have been hit by lift trucks
repeatedly.
Recommendation:
Replace with larger door.
13. FIBRECLAIM SCREEN SUPPLY PUMP
The screen supply pump, an AN Pump, is misapplied.
We have experienced plugging of the pump with strings.
Recommendations:
a. Cut out every other vane in the impeller
done July 9.
b. Close up spaces in VR Classifiner which allow
.material to pass - done July 12,
14. EXCESSIVE POWER ON VR CLASSIFINER SUPPLY PUMP
The VR Classifiner Supply Pump draws excessive power
when the valve is opened any appreciable distance.
Recommendation:
Slow pump so valve can be opened wider . - dohe July 12,
361
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FKANK1.1N SOLID WASTE PLANT PROBLEMS ' Pago 5
1 b . Dl FK I CULT IKS IN SECONDARY SCHEMING
The 12P screen is difficult to control - inlet
pressure may be too low.
Recommendation: «,
Temporarily bypass rejects ,"rom 24 P to Gyro-Pa -.',-^
done July 12.
. Also study 12P situation.
16 . DISPOSAL OF UNPULPABLES ' '
A. Tires
MCD does not want tires in landfill.
Recommendation :
Send tires to Franklin's old landfill.
B . Wood
% ,
MCD does not want to bury wood. Wes Flower will
check on burning. Meanwhile we will send lo
Franklin's old landfill.
t
17. VEHICLES
We are being plagued with flat tires on both the
loader and the fork lift.
Recommendation:
Go to solid tires.
18. WHITE VJATER CHEST AGITATOR
Internal bearing is gone on the white water chest
agitator.
Recommendation:
Replace with a different design bearing. In progress
J. D. Shafer.
362
PGM/crb
July 13, 1971
-------
W. Herbert
From Paul G. Marsh
July 9 1971
Copio* To R. F. Vokes
Subject Franklin Plant Operation -
Week of June 28 to July 3, 1971
file R»f.
plant Operation/
Statur,
anklin, Ohio Plam
During the week of July 3, most of the refuse was processed
directly in the Hydrasposal System. However, during the
week we worked on the start-up of the Fibreclaim System.
The first fiber was produced in the Fibreclaim System on
July 1, 197.1. This was a very small quantity due to
problems with pump power and plugging screens. After
making changes on July 2, we again ran the system on
July 3. Screen plugging problems did not appear to be a
serious problem. However, more work has to be done on
pumps.
In the Hydrasposal area, we operated with one set of broken
hamraera a 1.1 week. On Saturday, July 3, we cleaned out the
pulper and examined the tackle. We found that the stators
were in excellent condition. Other elements of the pulper
grinding tackle appeared to be too soft. We have proceeded
to order harder materials and to make other necessary
changes. My impression is that our problems in this area
are not serious.
I have attached a sheet containing operating statistics for
the week.
PGM/erb
Enc.
Status - Hydrasposal/Fibreclaim
Week of June 28 to July 3, 1971
363
-------
STATUS - llYDRASronAL/FIBRECLAIM
WEEK OF JUNE "28 TO JULY 3, "1971
Refuse Processed
Fiber Recovered
Magnetic Metal Recovered OD Basis
Non-Magnetic Metal OD Basis
Cyclone Rejects
Water
Organic Material
Pulpcr Operating Time
Reactor Operating Time
23,0 Tons (46 T/D on a 5-day/wcek
basis;
•»
200 Pounds
0.2% BOR* *
4.8% BOR
11.4% BOR
25% BOR (estimated)
51% BOR
44.6 Hours
39.5 Hours
* BOR = Based on Refuse
PGM/erb
July 9, 1971
364
-------
FILES
From
R. F. Yokes
June 1, 1971
To w- Herbert, P. G. Marsh, D. H. Kohlhepp
Franklin Plant Start-up — Status
Tueoday, June 1, 1971
... Solid Waste Processing/
Franklin Plant
Fluid Bed Reactor; Sand -- first Icac dried, ^ :>c..vri
-------
THE BLACK CLAWSON COMPANY
Shartle/Pandia Divisions
Middletown, Ohio
NOTICE
FRANKLIN PLANT START-UP
On Saturday, May 22, paper stock -was fed through the Hydr--
sposal System at Franklin, up to the fluid bed burner.
Only minor problems were encountered, and these have now
been corrected.
The fluid bed burner was fired up on Wednesday, May 26
for drying out. The drying out, curing and loading with
sand will occupy the balance of this week and most of next
week. f
Next week we plan to run some garbage through the system,
up to the burner.
On Monday, June 7, we plan to run garbage through to the
burner, and to start fiber recovery the following week.
William Herbert
Solid Waste Systems Department Manager
sja
May 27, 1971
Distribution: Bulletin Boards
Department Heads
Plant Supervisors
Territorial Sales
366
-------
THE BLACK C L A W S 0 N COMPANY
Shartle/Pandia Divisions
Middletown, Ohio
• FRANKLIN STATUS REPORT
The Franklin plant went into full production on
Monday* June 21. After a week of satisfactory
—operation, the Franklin landfill was shut down
-on the 28th, and we are now processing all of the
--waste delivered. . . . .
The plant is operating at design rate ~ 50 tons
per eight (8) hours. . :
—The "fiber recovery plant will start this .week.
William Herbert
•Solid Waste Systems Department Manager
6/30/71'
kr
367
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FOR MORE 1NFORMAI :<3N ABOUT THE FRANKLIN PLANT
Herbert, W. Solid waste recycling at Franklin, Ohio. In
Proceedings; Third Mineral Waste Utilization Symposium,
Chicago, Mar. 14-16, 1972. U.S. Bureau of Mines and
Illinois Institute of Technology "Research Institute.
Herbert, W., and W.A. Flower. Glass and cliumnum recovery in
operations. Publicjtorks, 102(8):70, 110, 112, Auj. 1971. Reprinted,
[Cincinnati], U.S. Environmental Protection Agency. 1972. 2 p.
(Environmental Protection Publication SW-96.J.)
Herbert, W., and W.A. Flower. Waste processing complex emphasizes
recycling. Public Works, 102(6):78-819 June 1971. Reprinted, [Cin-
cinnati], XJ.S. Environmental Protection Agency, 1972. & p.
(Environawntal Protection Publication SW--97»j«)
Neff , N.T. Solid waste and fiber recovery demonstration plant for the
^elty of Franklin, Ohiot an interim report. Environmental Protection
Publication SW-47d.i. U.S. Environmental Protection Agency, 1972.
83 p. (Distributed by National Technical information Service,
pringfield, Va. , as-- fB-213 646.0
,. • -
Neff, N.T. Solid waste and fiber recovery demonstration plant .<%.OT the
city of Frariklin, Ohio; final report, v. i, 2. U.'S.. Environmental
Protection Agency, 1974. (In pass/*;- to be distributed by National
Technical Information Service., Springfield, Va.)
ms
368
230Gc'\;'hD.'->
o, Elinor C:
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