Document Znjyx5VdEB1j3NLQb7NLnKOOd

CEA 1430 & 1800 Date: August 28, By: R. S. Yates Page 1 1967 1.1TITLE Aroclors - Increase Aroclor Capacity - Organic Division At Anniston Plant - CEA 1430 At WGK Plant - CEA 1800 1.2_SUMMARY The objectives of this project are to, a) Provide finished floods storage facilities at AnnistoiiandwSirK'assure 1 a minimum inventory of the various Aroclors and Aroclor blends so that bulk shipments can be made on demand. b) Provide at Anniston for blending and djjumming of the several Aroclors witffT?ffi8T,ll*fcomponeCT?,,wfthout interfering with primary production facilities. c) Minim:ze potential for cross contamination of products. d) Provide loading facilities for tank lyjuck^ and tank-cars and unloading facilities"for jaw mater ials in tank cars. e) Provide additional raw material biphenyl and at Anniston for TJg and at WGK for Xl~- f) Provide at Anniston new expanded facilities for fleeing and bacjcjjLnc^ biphenyl and ^olid^ Aroclors ` l^ - IZ&A g) Provide new facilities at WGK to increase plant capacity from 29.5M lbs./year to 69.5M lbs./year. h) Provide an overall production capacity for liquid Aroclors of up to 30% more than indicated in the latest Sales forecasts. Pjflitijjf for an orderly expansion of the WGK and Anniston A ro c 1 o r "iTaciYl t lesT"-1** Addition of these facilities will result in capacity increases over the present standard'1' capacity as follows: 03^6000 TOWOLDMONOQ44312 1.3 1.31 At WGK, At Anniston, CEA 1430 & 1800 Date: August 28, Page 2 Liquid 40.0M Liquid 5.7M Solid 1.0M lbs./year lbs./year lbs./year 1967 I (1) Note - Standard capacities at present are: At WGK, Liquid 29.5M At Anniston, Liquid 48.0T! Solid 10. lbs./year lbs./year lbs./year The installation at Anniston will include finished storage and blending tanks, two flakers for solid Aroclors and biphenyl, a drumming station, tank car spur and loading facilities and bagging station for solid Aroclors and biphenyl. The installation at WGK will include a new continuous chlorination line, blow tank, intermediate storage, distillation equipment, continuous clay treatment facilities, finished storage tanks, and a biphenyl storage tank with additional rail spur and unloading docks. Desired completion dates: Tank farm at WGK Tank farm at Anniston Flaking facilities at Anniston New production facilities at WGK July 1, 1968 August 1, 1968 September 1, 1968 December 1, 1968 PROCESS TECHNOLOGY Process Description Aroclors are the reaction products formed by the chlorination of biphenyl and/or terphenyls using an iron catalyst. The by-product HCl gas produced is absorbed in water to produce muriatic acid. Crude Aroclors are produced in chlorinator reaction vessels, air blown and distilled. Liquid Aroclors are earth treated, filtered and loaded for shipment. Solid Aroclors are drummed, flaked or flaked and milled and packaged for shipment. Distillation residues are discarded as waste or sold as Montars. A numerical system of nomenclature is used for iden tifying the various Aroclors. 0346001 TOWOLDMONOQ44313 1.32 CEA 1430 & 1800 Date: August 28, 1967 Page 3 Product yields are calculated on both chlorine and biphenyl and are different for each plant and for each Aroclor produced. They are recorded in the respective plant cost standards. Process documents: "Standard Operating Instructions for Aroclors Anniston Plant" - April 1966 - M. J. Williams "Standard Manufacturing Process for Aroclors Anniston Plant" - September 1966 - M. J. Williams "Process Description for the Manufacture of Aroclors - Department 246 - WGK Plant" - October 1966 D. E. Harris "Process Description for the Manufacture of Pyranols and Inerteens - Department A246 - WGK Plant" October 1966 - D. E. Harris "Standard Manufacturing Process for Pydraul A-200 Department B-246 - WGK Plant" - October 1966 D. E. Harris "Operating Instructions - Aroclor and Pyranols Departments 246 and A246 - WGK Plant" - August 1966 - V. Brawley "Final Report on the Continuous Chlorination of Biphenyl" - June 4, 1957 - R. A. Simone "Tentative Process for Continuous Chlorination of Biphenyl" - March 23, 1956 - R. A. Simone "Final Report on the Continuous Chlorination of Aroclors - Plant Demonstration" - May 7, 1958 R. A. Simone Raw Materials 1.321 Specifications Reference is made to the respective standard process manuals for raw material specifications. Raw materials at Anniston, for this project, are the Aroclors and additives used in blends and mixes and at the flakers. Raw materials at WGK are the materials used for the manufac ture of Aroclors. A list of materials follows: 0346002 TOWOLDMONOQ44314 CEA 1430 & 1800 Date: August 28, 1967 Page 4 Plant Material Code WGK (246) 82601 33500 38800 19409 43099 81059 Anniston (27) 82612 81102 82641 82613 82613 82614 82614 82615 36100 60200 58500 61320 - 64010 Date Material 12/8/64 1/7/66 7/21/66 1/21/66 2/18/65 6/29/66 Diphenyl Ferric Chloride, Anhydride Lime, Hydrated Attapulgus Earth 200/UP Nitrogen Gas Chlorine, Liquid 6/17/66 1/10/64 7/5/64 6/28/64 7/15/64 2/7/62 7/15/64 3/2/66 5/26/66 6/3/65 8/29/63 12/23/63 - 12/18/64 Aroclor 1242 Electrical Grade Aroclor 1248 Electrical Grade Aroclor 1248 Non-Electrical Grade Aroclor 1254 Electrical Grade Aroclor 1254 Non-Electrical Grade Aroclor 1260 Electrical Grade Aroclor 1260 Non-Electrical Grade Aroclor 1262 Glycidyl Phenyl Ether (1) Trichlorobenzene (1) Tetrachlorobenzene (1) Epoxide 201 Toluene Xylene (1) WGK Specification 1.322 Sources WGK Biphenyl Received from the Anniston Plant in 20,000 gallon unlined steel, steam heated tank cars. Transferred to an existing 25,000 gallon storage tank. Chlorine Received direct from WGK's Department 232 in a 4" transfer line. This line is being replaced by a 6" transfer line in the third quarter of 1967. Ferric Chloride Received from the warehouse in 2 lb. glass containers. Lime, Hydrated Received from the warehouse in 100 lb. bags. 0 346003 TOWOLDMONOQ44315 1.33 CEA 1430 & 1800 Date: August 28, 1967 Page 5 Attapulqus Earth Received from the warehouse in 50 lb. bags. Nitrogen Gas Supplied by a bulk station located in the tank farm area. Anniston Aroclors are transferred by pipeline direct from department to storage and from storage tanks to mix tanks, to drumming station and to flakers. Glvcidyl Phenyl Ether Received from the warehouse in 55 gallon drums. Trichlorobenzene Received from Hooker Chemical Company in 8,000 gallon steel tank cars. Tetrachlorobenzene Received from Hooker Chemical in 8,000 gallon tank cars. Epoxide 221 Received from warehouse in 55 gallon drums. Toluene Received from warehouse in 55 gallon drums. Xylene Received from warehouse in 55 gallon drums. Products and By-Products 1.331 Quality Considerations Marketing stresses that quality protection is the most effective means of protecting our present sales position of electrical grade Aroclors. Plant studies have shown that the use of aluminum tanks and aluminum transfer piping systems coupled with inert blanking of in-process and finished goods storage tanks will give us maximum protection. 03<i600'i TOWOLDMONOQ44316 CEA 1430 & 1800 Date: August 28, 1967 Page 6 1.332 Specifications Reference is made to the respective standard process manuals for finished goods specifi cations. Finished products at Anniston, for this project, are the completed blends from mix tanks and solids from the flakers. At WGK, finished products, are the liquid Aroclors and Montars. A list of products follows: Product Code Anniston Date Product Code WGK Date Product 82611 82612 82612 81102 82641 82613 82613 82614 82614 82615 -- -- 82622 82621 82620 82619 82618 82616 82601 82649 82658 82681 82659 82661 82685 82664 10/28/63 6/17/66 7/15/64 1/10/64 7/15/64 6/28/65 7/15/64 5/25/66 6/15/64 3/2/66 7/15/64 7/15/64 3/11/66 3/15/66 3/11/66 3/11/66 3/11/66 3/11/66 7/8/65 4/18/66 4/18/66 5/3/67 3/11/66 3/15/66 3/9/66 4/17/58 8115 81101 81101 81102 81102 81103 81103 81105 81105 81107 82868 82868 4/7/64 6/17/66 7/15/64 1/10/64 7/15/64 6/28/65 7/15/64 5/25/66 6/15/64 3/2/66 7/15/64 7/15/64 Aroclor 1232 Aroclor 1242 Electrical Grade Aroclor 1242 Non-Electrical Grade Aroclor 1248 Electrical Grade Aroclor 1248 Non-Electrical Grade Aroclor 1254 Electrical Grade Aroclor 1254 Non-Electrical Grade Aroclor 1260 Electrical Grade Aroclor 1260 Non-Electrical Grade Aroclor 1262 Non-Electrical Grade Montars 1, 2 Montars 314 Aroclor 5460 Aroclor 5442 Aroclor 5060 Aroclor 4465 Aroclor 2565 Aroclor 1268 Biphenyl Inerteen PPO A13B3B Inerteen 54201 KA Aroclor 1260 - 10% Toluene Aroclor 1262 - 10% Toluene Therminol FRO Aroclor 1254 - 10% Toluene 1.333 Packaging and Shipping Liquid Aroclors At both Anniston and WGK, liquid Aroclors are shipped in the following manner: Tank Trucks Size - 4,000 gallon Materials of Construction - All electrical grade Aroclors are loaded into SS trailers. Non-electrical grade Aroclors may be shipped in steel trailer tanks. 03<.6006 TOWOLDMONOQ44317 CEA 1430 & 1800 Date: August 28, 1967 Page 7 Tank Cars Size - 4,000 or 8,000 gallon Materials of Construction - All electrical grade Aroclors are loaded into solid aluminum cars or in tin, zinc or aluminum spray-lined cars. Non-electrical grade Aroclors may be shipped in steel cars. Drums and Cars Size - 5, 30 or 55 gallon Materials of Construction - Lacquer-lined containers. Solid Aroclors At Anniston, solid Aroclors are packaged in 5 and 40 gallon galvanized steel drums as a solid and in 41 gallon fibre drums as flakes. Biphenyl and Aroclor 5460 are packaged in bags as follows (major part of the production): Bags Aroclor 5460 Net weight - 100 lbs., St. Regis No. PCBG-32A. Size - 18" X 6" X 34" with a 5" valve. Type - Sewn Valve (SV). Biphenyl Net weight - 50 lbs., St. Regis No. PCBG-145A. Size - 16-3/4" X 5" X 33" with 5-1/2" valve. Type - Sewn Valve (SV). HB-40 At Anniston, HB-40 is packaged in 5 and 55 gallon steel drums. 1.34 Waste Streams ' WGK 1,250 lbs./day of HC1 gas absorbed in a 50 GPM water stream (0.21%) will be discharged from the continuous blow tank into the plant sewer. Other process losses are of a minor nature. 0346006 TOWOLDMONOQ44318 1.35 CEA 1430 & 1800 Date: August 28, 1967 Page 8 Anniston No change is expected in waste discharges as a result of this project. A dust collector will be installed to control Aroclor dusts from the milling operation of Aroclor 1268. Personnel, Property and Public Hazards Chlorine Gas Causes eye, skin and mucous membrane irritation. In strong concentrations canister gas masks, Scott Air Paks, or oxygen breathing apparatus are required. Biphenyl Solid at normal temperatures. Fumes are toxic over a prolonged period of exposure. The flash point is 235 F. HCl Gas Fumes are very toxic and hazardous to teeth, skin, eyes and mucous membranes. In strong concentrations, rubber protective equipment and approved pack or cannister gas masks are required. Ferric Chloride Solid at normal temperatures. Material is not toxic but presents an eye hazard. Xylene Fumes are very toxic. Limiting explosion concentra tion is 1.27 to 7.0% by volume in air. The flash point is 40F. Trichlorobenzene Solid at normal temperatures. Fumes are medium toxic. Fire point is above 210 F. Crude Aroclors During processing,Aroclors are generally hot, 100 C or above, and can cause serious thermal burns. Con tinuous or repeated skin contact must be avoided. Vapors at room temperatures should not be breathed in a confined space. At elevated temperatures, fumes are quite toxic. Continuous or repeated skin contact with Aroclor must be avoided by the use of gloves and protective garments. ' 03A6007 TOWOLDMONOQ44319 CEA 1430 & 1800 Date: August 28, 1967 Page 9 1.4 MANUFACTURING FACILITIES 1.41 Description 1.411 General The following information is included in the Appendix of this report: Equipment Flow Sheets Suggested Equipment Layout Equipment Lists Scopes of Work Preliminary Schedule Project Loss Prevention Report 1.412 For Anniston New storage and blending tanks to be added: Aroclor 1242 It 1248 II 1254 II 1260 II 1262 II 1221/1232 Inerteen PPO and A13B TCB TTCB 54,000 gallon 18,000 1 54,000 II 18,000 II 18,000 II 18,000 II 30,000 12,000 12,000 II II II (2 - 27,000 gallon) (2 - 27,000 gallon) (1 - 12,000 gallon) (1 - 18,000 gallon) An existing 2,000 gallon mixing tank will be relocated. One covered loading dock for tank cars. One covered loading dock for tank cars and trailers. A new railroad spur. Four existing 12,000 gallon storage tanks with submerged pumps will be dismantled and scrapped. New drumming facilities to be added include a high speed drumming scale and a conveyor system to bring empty drums to the scale and take filled drums away from the scale. New flaking and bagging facilities to be added: Storage for Aroclor 5460, 1268 and biphenyl . Flaker for solid Aroclors ' 0346008 TOWOLDMONOQ44320 CEA 1430 & 1800 Date: August 28, 1967 Page 10 Flaker for biphenyl Mill for Aroclor 1268 High speed bagging machines for Aroclor 5460 flakes and biphenyl flakes Conveyor system to take filled bags away from bagging machines Fume control system for Aroclor 1268 The existing Aroclor and biphenyl flakers will be dismantled together with the present Aroclor feed tank. A suitable building (120' X 60') to house the drumming and flaking operations. Pipelines from Department 27 to tank farm as follows: One line for Aroclor 1242 from existing 12,000 gallon day tank One line for Aroclor 1248 and 1221 One line for Aroclor 1254 from existing 12,000 gallon day tank One line for Aroclor 1260 One line for Aroclor 1262 Pipelines from tank farm to mix tanks: One line for Aroclor 1242 One line for Aroclor 1254 One line for Aroclor 1260 One line for Aroclor 1248 and 1262 Pipelines from tank farm to loading spots and drum filling: One line for A13B One line for KA and PPO One line for Xylene and Toluene blends (drum filling only) 0346009 TOWOLDMONOQ44321 CEA 1430 & 1800 Date: August 28, 1967 Page 11 One line for HB-40 (drum filling only) One line for Aroclor 1242 One line for Aroclor 1254 One line for Aroclor 1221, 1232, 1248, 1262 One line for Aroclor1260 Pumps will be providedas follows: One for Aroclor 1242 transfer at tank farm One for Aroclor 1254 transfer at tank farm . One for Aroclor 1248/1221, 1232/1262 trans fer at tank farm One for Aroclor 1260 transfer at tank farm One for Mix tank and PPO tank transfer One for Xylene Mix tank transfer One for TCB, TTCB tank car unloading One for TCB, TTCB transfer to Mix tank Three to transfer Aroclors from Building 27 to storage 1.413 For W. G. Krummrich New storage tanks to be added: Aroclor 1242 Aroclor 1248 Aroclor 1254 Aroclor 1260 Biphenyl 44,000 gallon (2 - 22,000 gallon) 22,000 gallon 22,000 gallon 22,000 gallon 100,000 gallon A new railroad spur Two unloading docks for biphenyl cars Three existing 15,000 gallon storage tanks with submerged pumps will be dismantled. Pipelines from day tanks to tank farm as follows: 0346010 TOWOLDMON0044322 CEA 1430 & 1800 Date: August 28, 1967 Page 12 One line for Aroclor 1242 One line for Aroclor 1248 One line for Aroclor 1254 One line for Aroclor 1260 Pipelines from tank farm to loading spots and drum filling: One line for Aroclor 1242 One line for Aroclor 1248 One line for Aroclor 1254 One line for Aroclor 1260 Pumps will be added as follows: One for Aroclor 1248 transfer One for Aroclor 1254 transfer One for Aroclor 1260 transfer One for Aroclor 1242 transfer Facilities to produce 40M lbs./year of Aroclor 1242: A continuous chlorinator chain consisting of biphenyl mix and continuous feed tank, four chlorination tanks, four mass circulating pumps and four external air coolers. A continuous blow tank and intermediate storage tank. Two semi-continuous distillation systems consisting of still pot, external circulat ing system with therminol heating, entrain ment separator, vapor condenser, receiver and vacuum steam ejector. Two continuous porocel treatment systems consisting of feed tank, absorber, cleanup filter and product receivers. One train will have two absorbers to provide flexi bility . 0346011 TOWOLDMONOQ44323 1.42 . CEA 1430 & 1800 Date: August 28, 1967 Page 13 A complete therminol heating, storage and circulating system. Additions to the existing control room to provide space for a foreman and motor con trol center. Design Capacity 1.421 Anniston Finished Product Storag e Recommended ^ Provided Product (gal.) (gal.) Future Need (gal.) (1970) 1221 1232 1242 1248 1254 1260 1262 TOTAL 13,050-1 14,000J 97,500 20,800 51,500 20,900 5,550 223,300 18,000 66,000(2) 18,000 66,000 18,000 18,000 ' 204,000 27,000 27,000 Increased flexibility in the storage area will allow a apacity increase of 5.7M lbs./year (from 48M to 53.7M). Estimated tank car shipments for 1971: Estimated tank trailer shipments for 1971: Estimated drum shipments for 1971: Estimated can shipments for 1971: 372. 66 25,610 2, 030 (3) (3) (3) (3) (1) Letter from HJD to RSY 5/18/67. (2) Includes 12,000 gallon of day storage. (3) Anniston Job No. 370-720 (1) by R. H. Taylor Mixing and Drumming Area A new 12,000 gallon mix tank, a relocated 2,000 gallon mix tank and an 18,000 gallon mix tank to provide for: Estimated tank car shipments for 1971: Estimated tank truck shipments for 1971: Estimated drum shipments for 1971: Estimated can shipments for 1971: 55 1 5,764 1,312 (3) (3) (3) (3) A new drumming station with associated conveyors to handle 150 drums/day. (Basis: 8 hrs./day, 260 days/year, 75% OST) 0346012 TOWOLDMONOQ44324 CEA 1430 & 1800 Date: August 28, 1967 Page 14 Flaking and Bagging Aroclor flaking capacity (Aroclor 5460) 41,500 lbs./day (Basis: 8 hrs./day, 365 days/year, 75% OST) Aroclor bagging capacity 2 bags/min. Biphenyl flaking capacity 18,300 lbs./day (Basis: 8 hrs./day, 365 days/year, 75% OST) Biphenyl bagging capacity 2 bags/min. Flaking and bagging design will allow these operations to be carried out on a one-shift basis, seven days a week. Exception is Aroclor 1268 which will be flaked and packaged on a three-shift basis, seven days a week (3% of production). Raw Material Storage Raw Material Provided (gal.) TTCB TCB 12,000 12,000 1.422 WGK Finished Product Storage Recommended Product (gal.) 1242 1248 1254 1260 TOTAL 132,000 25,200 34,400 20,200 211,800 Provided Future Need (gal.) (gal.) (1970) 84,000 ^ j 42,OOO 3 42,000 ' 22,000 190,000 66,000 66,000 Estimated tank car shipments for 1971: Estimated tank trailer shipments for 1971: Estimated drum shipments for 1971: Estimated can shipments for 1971: 112 306 12, 200 765 (1) Letter from HJD to RSY 5/18/67. (2) Includes 40M gallons on hand storage (3) Includes 20M gallons on hand storage. Extra storage required for operating flexibility. (4) Include 20M gallons on hand storage. 03<,bOV3 TOWOLDMONOQ44325 CEA 1430 & 1800 Date: August 28, 1967 Page 15 Raw Material Storage Raw Material Biphenyl Provided (gal.) 125,000(5) (5) Includes 25M gallons on hand storage. Provides capacity for 4 - 20,000 gallon cars and six days' supply at increased rate. New unloading track and docks provide four days turnaround time at increased rate. New Manufacturing Facilities Continuous chlorination: Basis: OST; Rate: Producing Aroclor 1142 7,950 hrs./year 43M lbs./year Semicontinuous distillation and earth treatment: Basis: OST: Rate: Producing Aroclor 1242 7,^50 hrs./year 40M lbs./year For the overall product group, after these additions are completed, Anniston and WGK plant capacity will be as follows, H lbs./ year: Present Capacity New Capacity Increase in Capacity Anniston WGK 48.0 29.5 TOTAL CAPACITY 77.5 53.7 69.5 123.2 5.7 40.0 45.7 Based on 1971 requirements for both plants (July 1967 Sales Forecast), excess capacity at that time will be: New Capacity Required in 1971 Excess Capacity 123.2M lbs./year 99.2M lbs./year 24.0M lbs./year Excess Capacity 24.2% 0346014 TOWOLDMONOQ44326 CEA 1430 & 1800 Date: August 28, 1967 Page 16 1.43 Flexibility Requirements 1,431 Anniston Increased storage capacity and blending facilities will allow for better utilization of present still capacity. This will be accomplished by longer runs on the same product and result in increased pro duction capacity. ` 1.432 WGK Based on the sales forecast of July 1967 for the Aroclor product group, batch units will produce Aroclors 1248, 1254 and 1260. The maximum capacity of these units is as follows for each Aroclor: Aroclor 1248 8,750 hrs. X 7,200 lb./ba. X 5 chlor X 92% OST = 34.4 M lbs. 8.5 hrs.7ba. Aroclor 1254 8,750 hrs. X 8,040 lb./ba. X 5 chlor X 92% OST = 30.8 M lbs. 10.5 hrs./ba. Aroclor 1260 8,750 hrs. X 9,100 lb./ba. X 5 chlor X 92% OST = 29.2 M lbs. 12.5 hrs./ba. For the year 1971, the maximum batch capacity will be: For Aroclor 1248: 34.4 M lbs. X 21%(1'= 7.25 M lbs.. For Aroclor 1254: 30.8 M lbs. X 35%^1)= 10.80 M lbs. For Aroclor 1260: 29.2 M lbs. X 43%^L)= 12.60 M lbs. Total Batch Capacity on this basis = 30.65 M lbs. (1) From the July 1967 Sales Forecast for 1971. 0346015 TOWOLDMONOQ44327 1.44 . CEA 1430 & 1800 Date; August 28, 1967 Page 17 Requirements for 1971 are 20.3M lbs., leaving an excess capacity of 51% at WGK. For 1971, the continuous system capacity utili zation will be 25.6M lbs., leaving an excess capacity of 56% at WGK. Flexibility will be designed into the WGK dis tillation systems to allow for the following operations: Still No. 1 (existing) Aroclor 1260, 1262 Still No. 2 (existing) Boil down still to separate Montars (residues) from all products, Aroclors 1242, 1248, 1254, 1260 and 1262. Still No. 3 (New) Aroclor 1242 or 1254 Still No. 4 (New) Aroclor 1242 or 1254 Future Expansion 1.441 Anniston At the completion of this expansion, space will be available to the north of Building 27 for the addition of a complete new solid Aroclor line. Space is avail able in the tank farm area for additional tankage. Flaking and drumming capacity can be increased by adding additional personnel and operating on a 2 or 3 shift basis. 1.442 WGK One of the objectives of this expansion is to provide 25-30% excess production capacity for Aroclors. As we use up the excess capacity provided in this project we must consider the next step in department expansion. If we assume the product split will increase propor tionally according to the latest sales forecasts,we can postulate an operation diagrammed as follows: 03A6016 TOWOLDMONOQ44328 CEA 1430 & 1800 Date: August 28, 1967 Page 18 1.45 The layout of the new chlorination-distillation facili ties at WGK will allow space for the addition of another chlorination unit, intermediate storage tanks and two additional distillation chains. Aroclor 1248 and 1262, because of the smaller requirements, would continue to be made in the batch units. On this basis, we can postulate a^ productive capacity as follows for liquid Aroclors, M lbs./year: Anniston WGK batch units Cont. 1242 unit Cont. 1254 unit Cont. 1260 unit 53.7 29.5 40.0 15.0 15.0 TOTAL CAPACITY 153.2 Physical Appearance 1.451 Anniston Tanks of different heights will be grouped together to provide standardization. In the flaking and drumming area, provision will be made for moving finished products directly into a new warehouse facility (when built). 03'i6017 TOWOLDMONOQ44329 1.46 . CEA 1430 & 1800 Date: August 28, 1967 Page 19 1.452 WGK Tanks will be grouped together as an exten sion of the present tank farm. The new facilities will be a separate structure to the south of the existing unit. Storage and Shipping Requirements 1.461 Anniston Facilities provided are noted in greater detail in other parts of this report. Provision is being made for: Raw material storage of TTCB and TCB. Finished product storage for all liquid Aroclors. Loading docks for tank car and tank trailer loading of products. Moving filled bags of solid Aroclors and biphenyl to palette loading station, then to warehouse storage. Moving drums and cans to palette loading station, then to warehouse storage. Storage in the drumming area of the new manufacturing facility for empty drums and containers. 1.462 WGK Provision is being made for: Raw material storage of biphenyl. Finished product storage for all liquid Aroclors. Unloading docks for tank cars. Making an existing unloading dock a loading dock for tank cars of Aroclors. No extensions or additions are being made to the present blending and drumming facilities. WGK technical service is modifying an existing storage tank to a blend tank and revamping piping in the drumming area. 0346016 TOWOLDMONOQ44330 5 1.51 CEA 1430 & 1800 Date: August 28, 1967 Page 20 UTILITIES AND SERVICES Utility and Service Requirements 1.511 Anniston Additions / Steam - 100 psiq-For Storage Tanks 2,000 lbs./hr -For Process 500 lbs./hr y Purchased Water- For Process (Cleanup) 150 GPM V Compressed Air - For Storage Tanks y Plant Water - For Process (Flakers) y Nitrogen - For Storage Tanks 20 GPM 300 GPM 50 SCFM Electric - Connected 300 HP - Operating 200 HP 1.512 WGK Additions Steam - 80 psiq - For Storage Tanks 5,000 lbs./hr - For Process 3,000 lbs./hr 200 psig-For Process Natural Gas - For Process 600 lbs./hr 1,800 SCFH Purchased Water- For Process 150 GPM Compressed Air - For Process 100 SCFM Electric - For Instruments - Connected - Operating 75 SCFM 315 HP 250 HP Plant Water - None Required Nitroqen - None Required Utility and Service Facilities 1.521 Anniston A new spur track from main track at north of plant to 5th Street, 1700 ft. long. 0346019 TOWOLDMON004433T CEA 1430 & 1800 ' Date: August 28, 1967 Page 21 A new 300 KVA pole line transformer to supply tank farm and warehouse requirements. A new sewerage lift station to replace existing field which is in the proposed manufacturing area. The lift station will tie into an exist ing city sewerage line. Relocating a 24" IPS VC acid sewer. Installation of a steel frame prefab-type building, 120' long X 60' wide to house the flaking, drumming and bagging facilities. This building will be designed so that it can be attached to a new warehouse building which will be 120' wide X 240' long. A 15' wide X 80' long tank truck loading sta tion. Relocation of existing plant parking facilities 70' wide X 120' long. 1.522 WGK Extension of existing track 10A for 110 feet and installation of a turnover to tie existing track 10A into track 10. ' Replace existing gas meter with a larger capa city meter. Install new pump at department city water break tank with associated piping. Install new 600 amp breaker in Sub #17. Install fans in Sub #17 transformer. Transfer feeder 8-1 from Sub #8 to Sub #17. Install an overhead feeder from Sub #17 to Building CF. Install feeder cables from breaker 8-1 to Department 246. 0346020 TOWOLDMONOQ44332