; :>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;-- •.- --.
                 , _, .  •    Region V, JlV-'T'v     '    -'•'--'
    iisleo-y- to public    Om~    ,' ' '   -7        ,i
                         »50 Sout2i D-.:tr->-- :•-,-...:, j
                             go, minoto co:';;   	
                                                        20. .._, r/.  > .
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                                                             I ".' i  '.

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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.
                                111

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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.
                                   59

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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
                                   60

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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.
                                   61

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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
                                    62

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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
                           63

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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.
                                    65

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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
                                    66

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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
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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.
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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:
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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
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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)
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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.
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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.
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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
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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
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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

-------
     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,.

-------
                      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

-------
     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

-------
               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

-------
A - OPERATING DATA SUMMARY
        (48 PAGES)
             85

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Sheet 33

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B - ANALYTICAL DATA SUMMARY
            145
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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

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         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

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         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

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Figure 1.   Waste Load Variation
                              155

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Figure 2.   Rejects to Landfill
                              156

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                           o  »   gi  -jj   JJ  g|

                                   	; 	
                                   i'ii
                          ' ' (!»•» •'»'' ""3) 1ROI3J1 ISO N3AO
Figure 3.    Reusable Paper Fiber Recovered
                                     157

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      E
Figure 4.   Proximate Analysis of Reactor Feed
                               158

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                    _1TT_LTJ i 	[__i
Figure  5.   pH Various Plant  Waters
                              159

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Figure 6.   Settleable Solids in Various Plant Waters (By Volume)
                               160

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                               "t i  (aain/ow) sanos aiavaixias -T—rt
Figure 6a.   Settleable  Solids  in Various  Plant Waters  (By  Weight)
                                   161

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Figure 7.   Biochemical Oxygen Demand of Various Plant Waters
                                162

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               i   r     '-•^•-•Tirrv	
                                     r-^-*'.T"4-H
Figure 8.   Total Dissolved Solids in Various Plant Waters
                                163

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Figure 9.   Total Suspended  Solids in Various Plant Waters
                               164

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                            —•T.--1V-..,	|
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                                              !   j

                                            •  w
                                            ^•T :
                           (j«Ti:/a>0 sonos oaAiossia TVIOI I :
                       I  i
Figure  8.    Total  Dissolved Solids in Various Plant  Waters
                                   163

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Figure 9.   Total Suspended  Solids in Various Plant Waters
                               164

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Figure 10.   Total Volatile Solids in Ash Slurry
                                 165

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Figure 11.   Total Solids in Ash Slurrv
                                166

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Figure 12.   Junk Remover Rejects Non-Magnetic Fraction
                              167

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Figure 13.   Cvclone  Rejects  Analysis
                                 16ti

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     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

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             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

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             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

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                      (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

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                 (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

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APPENDIX A - BOWSER-MORNER REPORTS
            (60 PAGES)
                 174

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                                                                                        £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

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\. 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

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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

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                                 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

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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

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                                 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

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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

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                                 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

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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

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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

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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

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                                 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

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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

-------
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

-------
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

-------
                                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

-------
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

-------
                                 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

-------
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

-------
                                  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

-------
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

-------
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

-------
                                 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

-------
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

-------
                                   .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

-------
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

-------
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

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                                 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

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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

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 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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

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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

-------
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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

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                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

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         £\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

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                     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

-------
           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.

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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,

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 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

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          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

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                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

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      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

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  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:

-------