Document JNkEw8b7q78MLQapdqkzoNqNO

SAFETY - A. H. Sather Occupational Injuries July 1981 Year-To-Date 1981 Year-To-Date First Aid Medical Case Restricted Workday Cases Restricted Workdays Lost Time ' 1 0 0 0 0 2k 3 0 0 0 35 12 1 3 0 Injuries By Department Vinyl Operations Compound Operations Maintenance Laboratory Receiving and Warehouse Office 0 0 1 0 0 0 3 6 15 1 1 1 12 11 21 3 0 1 Injuries By Type Cuts and Abrasions 1 13 Eye Injuries 02 Burns 0 10 Bruises 02 Strains and Sprains 0 2 Other 01 23 k 5 10 k k As of July 31 1981, the plant operated 757 days or 992,978manhours without a disabling injury. Safety Meetings The topic for July safety meetings was "Hand Injury Prevention". The slide and tape program "Think Before You Reach" was shown and discussed. New Module Outage A considerable amount of time was devoted to planning the shutdown checklist for the August 10, 1981 outage in the new module for expansion, maintenance and other engineering work. Fi re School J. R. McCrimon -Compound Operations Superintendant attended the Texas A & M Industrial Fire School J4ly 26-31, 1981. DTH 000021750 SAFETY - (continued) Phase III Firewater Project John Elkins - CED was in plant July 23, 1981 to review final equipment locations for Phase I I I of the plant firewater expansion project. Health Activity for the reporting period included routine monitoring for VCM, lead antimony and total particulates and a report of additional monitoring work done on plasticizers, tin, phthalic anhydride, chlorine and mercury. The results and overexposure are explained below. Chemical VCM Lead Antimony Total Particulates PEL Number Pe rcent Sb 97 5 100 5 100 3 100 PEL Number Percent 33 00 00 00 Overexposures Three exposures occurred to vinyl operating area personnel. One occurred to a vinyl supervisor during a VCM filter pack o-ring failure in the new module 9 one to a chief operator who was removing used VCM filters from the filter pack area and one to an "A" operator with no specific cause found. None of the above were wearing resp irators. Other Monitoring Additional monitoring was done on several other chemicals which were noted above. DIDP and 610P area samples were taken in ten locations with nine of the samples indicating less than 0.3 mg/m* and one at 3-3 mg/m* (610-P). There is no established standard for these chemicals. The OSHA standard for di 2-ethyl hexl phthalate is 5 mg/nr*. Four area samples and seven personnel samples for tin stabilizers indicated less than the detection limits. Several area samples for phthalic anhydride were taken on the charge floor of the plasticizer building and the results found to be less than 0.01 mg/m*. One phthalic anhydride per sonnel sample was taken on a yard operator during the unloading of a phthalic anhydride tank car. Several problems were encountered during the operation and the sample result indicated 0.7 mg/m'. A total of 13 Drager tube samples were taken during slug feeding of chlorine to the plant cooling towers. All samples indicated non-detectable results. Drager tube samples were taken in two areas for Mercury. The old I . E shop indicated results less than the detector tube detection limits. Sampling in the current I E shop indicated a result of 0.17 mg/m-* mercury following a small spill. The spill was cleaned up and the area was resampled with nondetectable results. DTH 000021751 VINYL - P. E. Markey Month Year to Date 1. Total Production, MM Lbs. 2. Production Rate, M Lbs./C.D. 3. Charges, Reactor Batches/C.D. 4. Total Charges 5. Reactor Stream Factor, % 6. Dryer Rate, Average Lbs./Hr. 7. Dryer Stream Factor 8. Accounting Days 23.5 765 20.2 628 90.4 5318 85.5 31 176.9 834 20.6 4372 87.5 5700 86.2 212 Vinyl Department production for July was 23.5 MM pounds or 94% of budget. Reactor and dryer stream factors were 90.4 and 85.5%, respectively. Reactors 1. Major repair work on D-400 agitator gear box resulted in a 2.4% reactor stream factor penalty. 2. Recovery and dryer imbalances resulted in a 3.1% reactor stream factor penalty. 3. Cleaning the condenser on 741 reactor resulted in a 0.6% reactor stream factor penalty. 4. Pluggage of the VCM charge header in the old module resulted in a 0.6% reactor stream factor penalty. 5. Replacement of both VCM charge valves on 743 reactor resulted in a 0.6% reactor stream factor penalty. 6. A main breaker failure in the old module resulted in a 0.35% reactor stream factor penalty. In order to better match sales and maximize operating costs efficiencies the production target for July was reduced from 27 MM pounds to 25 MM pounds. Two cost savings measures adopted were the use of a single rather than dual initiators in 5425 production and usage of a high productivity initiator in 5385. Dryers The vinyl unit was essentially reactor limited for the month as described above. DTH 000021752 VINYL - (continued) Resin Quality Summary Resin Type Prime Pounds "BC" Grade "H" Grade % of Total Product ion Budgeted Resin Product Slate, % 5305 5385 5425 5465 Sifter Overflow 4,381 ,474 13,836,560 4,998,941 109,180 - 29,250 214,000 100,950 - - 9,750 - 1 1 ,250 - (237,975) 18.8 59-9 21.8 0.5 ( 1.0) 3.9 70.6 22.2 3-3 N/A TOTAL 23,326,155 344,200 (216,975) 100.0 100.0 Quality performance for July was 99.4% customer grade with 1.5% "BC" grade and (0.9%) "H" grade. Variable Cost Performance The variable cost variances for July totalled a favorable $709 M with $619 M due to price and $90 M due to efficient operation. The major price variance was $612 M due to below budget monomer pricing. VCM pricing for the month was 21.084 i/lb. versus the budgeted 23.636 i/lb. The favorable $90 M efficiency variance is comprised of favorable variances of $44 M for processing additives, and $62 M in the off-grade category which resulted from intensive upgrading efforts. The favorable efficiency was partially off-set by a unfavorable efficiency of $19 M for VCM. Monomer consumption for the month was 1.022% pounds VCM/pound PVC versus the 1.01936 standard. The 108 VCM railcars weighed from Lake Charles in July showed an average shortage of 700 pounds per car versus the 650 pounds per car shortfall determined in June. Year to date VCM efficiency is 1.02215 pounds VCM per pound PVC. General 1. Packaging activities for the month totalled 1.7 MM pounds. 2. Resifting activities for profit improvement totalled 829 M pounds. 3. Operating problems associated with 5305 production using Chain Transfer Agents were resolved during the month with R&D technicial assistance. The problems appear to have been associated with residual AMS levels in the recovered monomer. A formula revision to solely fresh VCM has enhanced particle size control and no further problems have been encountered. Resolution of CTA problem and optimum uas of blend tank capacity resulted in 4.4 MM pounds of 5305 production. This represents the highest monthly production of this profitable resin on record. DTH 000021753 VINYL - (continued) General - (continued) 4. Trial production runs were successful in producing a 0.68 viscosity 5305 resin. This represents a key step in the development of improved fittings and bottle grade type resin. 5. Trial production runs were conducted with increased levels of calcium stearate in 5385 production. Batches were produced at 4 gallons, 8 gallons, and 16 gallons stearate levels. Samples were forwarded to PAL for testing. Further testing is planned for August. 6. An extended trial of the high productivity L-46 initiator was begun in July. Testing shows the L-46 initiator to be more active than L-223- However, reactor venting on L-46 is more severe than L-223 even at reduced initator loadings. DTH 000021754 COMPOUND - J. R. McCrimon Compound Production Montn Per Day Y.T.D. Line i, M Pounds Line V, M Pounds Line III, M Pounds Total , M Pounds Accountings 1,487 43 3,012 4,542 31 49.6 43-3 97.2 146.5 8,740 1 ,981 20,643 31,094 212 Line 1 operated 30 days during July at an average rate of 49.6 M pounds pe day. Major items affecting production efficiency were: product changes (45-3 hours), dicers (37-8 hours), blender conveyor (37-5 hours), bag charging resin (17-3 hours), quality control adjustments (8.0 hours), blender scales (5.9 hours), and blender conveyor clutch (5-5 hours). Line V operated 1 day during July at an average rate of 43-3 M pounds per day. Major items affecting production efficiency were: screw change (2.6 hours) and Orbitran (2.3 hours). Line III operated 31 days during July at an average rate of 97-2 M pounds per day. Line III production was affected by: product changes (40.3 hours), mill maintenance (9.0 hours), FCM (7-0 hours), dicers (6.6 hours), quality control (10.9 hours). Quality performance for flexible compound was 3-5% off-grade of which 76.8% was due to mill scrap. "BC" production was -2.98% (135 M pounds reblended). The raw material requirement for flexible compounds was 1.01037 pounds of raw material per pound of compound versus 1.01301 standard. (Y.T.D. is 1.00982) The variable cost variance for compound was $18.8 M with $48.9 M due to price and ($30.1 M) due to efficiency. The variance due to product mix was ($1.5 M), and the variance due to off-grade was ($35.2 M). There were no major efficience variances or price variances for the month. Dry Blend Month Per Day Y.T.D. Production, M Pounds Accounting Days 3,791 31 158.0 28,447 212 Dry Blend operated 24 days during July at an average rate of 158 M pounds per day. Production included 80273G, 80174, 90171, 80274, and RP-100 BW. Dry blend production was affected by: quality control (47-3 hours), product changes (21.8 hours), Brabender repairs (19-1 hours), and out of resin (5.7 hours). RP-100 BW and 90171 production to boxes also contributed to reduced rates. Quality performance for the month was 99-98% customer grade. DTH 000021755 COMPOUND - (continued) Dry Blend - (continued) The raw material requirement for dry blend was 1.00618 pounds of raw material per pound of dry blend versus a standard of 1.00576. (Y.T.D. is 1.01114) The variable cost variance for dry blend was $32.3 M with $24.8 M due to price and $7.4 M due to efficiency. The variance due to product mix was $21.9 M. There were no major efficiency variances and only one major price variance $11.4 M for titanium dioxide. Plasticizer Month Per Day Y.T.D. Production, M Pounds Accounting Days 805 50.3 31 7,205 212 Plasticizer operated 16 days during July at an average rate of 50.3 M pounds per day. Production included: D0P, DIDP, and 61 OP. VRP production totaled 72.9 M pounds (9-1%). Production was limited by: R-2 stub shaft repairs, R-2 vacuum valve replacement, R-4 safety disc replacement, and R-4 instrument repairs. Two other major factors limited plasticizer production: steam allocation due to boiler repairs and out of ALF0L 610 due to rejected shipment for high moisture. The raw material requirement for plasticizer was 1.06691 pounds of raw materials per pound of plasticizer versus a 1.10500 standard. (Y.T.D. is 1.11320) The variable cost for plasticizer was $9-1 M with $9.14 M due to price and ($0.04 M) due to efficiency. The only major price variance was $11.3 M phthalic anhydride and the only major efficiency variance was ($12.7 M) for phthalic anhydride. The variance due to product mix was ($1.7 M). General Total customer grade compound inventory increased from 8.9 to 10.1 MM pounds during July. Line I Banbury repairs are scheduled for August in order to reduce the mill scrap production rate. Two new compounds were produced for Belden du'ing July. DTH 000021756 MAINTENANCE - S. J. Vincent Vinyl There were no reactor seal failures in this period. One reactor condenser was cleaned and one gearbox experienced a failure. The condenser cleaned was on the 741 reactor in the new module. The gearbox failed on the D-400 reactor. The gearbox and seal housing had to be removed from D 400 reactor. The seal housing was sent out for sleeving and the gearbox was overhauled. The motor was also removed for a service check. The safety valves were tested and the safety discs were changed on both the D-300 and D-400 reactors in the old module. The VCM charge header in the old module from the filters to the charge meters was removed for cleaning. The VCM turbine meters were pulled and cleaned twice. There were five major valves replaced in this period. In the old module the inlet valve to the north VCM filter and the VCM charge valve on D-400 reactor were replaced. In the new module the slurry dump valve and the recovery valve were replaced on 741 reactor and the vent valve on 742 reactor. In the old module the south recovered VCM receiver was opened for cleaning and the south recovery condenser. The flow controller for "B" recovery compressor was replaced. The level control for D-300 and D-400 cooling tower was calibrated. There were fourteen repairs to pumps and compressors in the vinyl production area in this period. In the old module the recovered VCM charge pump and rinse pump were overhauled and then the spare "A" vacuum pump was installed. Seals were replaced in the east and west VCM return pumps, east and west VCM charge pumps, "A" compressor outboard seal, "A" vacuum pump inboard and outboard seals, 705 emission recovery compressor outboard seal and the 703 emission recovery vacuum pump outboard seal. In the new module the third recovery compressor was reinstalled and the seal replaced on the west chem-wash pump. Repairs to the vinyl drying equipment were to change out the #6 centrifuge and gearbox twice, and the #5 centrifuge and gearbox once. The repairs were the result of plugging and resulting plastic accumulation in the conveyor section. The drum drive gearbox on #2 dryer was overhauled with the drive sprocket and chain being replaced. Several blend tank level transmitters were checked. A major problem developed with the use of the Conoco HD calcium grease. Several bearing failures were directly attributed to the breakdown of this grease. Information has been received that indicates there may have been a blending problem with the HD calcium. Due to the recommendations of our equipment suppliers and the bearing failures experienced, an alternative grease has replaced the Conoco HD calcium and we are currently completing our stock changeover. DTH 000021757 MAINTENANCE - (continued) Compound, Dry Blend, Plasticizer and Resin Storage The major repairs in the compound area were to replace the FCM seals, rotary joints, the conveyor belt to the mill and the mill rotary joints on line three. The bucket clutch and flex line to the mill rotary joint were replaced on line one. Line I blender conveyor bucket continues to drop from its chain and cause problems. Dicer blades continue to be a major maintenance cost item for both compound lines. Two dicer motors were repaired. The dry blend unit was shut down to replace the #2 bowl and to repair the #1 Welex bowl. The switchgear was also serviced. The mixer blades were replaced in both Welex units and the screen was replaced in the south Kason screener. Several blender and feeder valves were repacked. Repairs to the plasticizer unit were to replace seals in the PA charge pump, tank 109 pump and to overhaul 110 tank pump. The safety disc was replaced on R-4 reactor. Utilities and Service There were six repairs to the plant air system compressors during this period. Valves were repaired twice in the #2 and #3 compressors and once in the #1 and //6 compressor. The plant breathing air system revisions were completed in this period. The //I and #3 boilers were shut down for inspection and repair. All boiler tubes were hydro-blasted, followed by chemical cleaning. There were two tubes plugged in #1 boiler and eight tubes plugged in #3 boiler. The refractory was repaired in both boilers. The tool room mechanics completed bench testing of the new safety valves for the relief valve modification and expansion projects. The plant machinest and air conditioning mechanics were very productive this month, machining parts and maintaining the plant air conditioning systems. Planner There were 78 work orders planned and estimated in this period. There were 22 registers closed and 23 new registers issued. Material was ordered for 26 projects. The planner worked with Tom Knuckles from MED on planning the upcoming new module shutdown. Miscellaneous Four mechanics were given- training in the operation of the plant crane. New columns have been installed in our plant gas chromatographs. The conduit and cable have been installed to add amp meters in the old module recovery system. The installation of the instrumentation for the spare inert vent incinerator has been started. New level controls were also installed in the dry blend use bins. DTH 000021758 MECHANICAL ENGINEERING - J. A. Dixon AFE's Submitted, Approved, and Closed The following AFE's were submitted and approved during July: AFE No. Title Authorized 9671 "^1-------- " 9691 9701 9711 9721 New VCM Railspu?2!7> Miscellaneous Projects Under $10,000 Reactor Agitator Two Speed Motors Miscellaneous Energy Savings Projects Under $10,000 Plasticizer Spill Containment Emergency Cooling for Reactors $194,000 145,000 40,000 25,000 42,000 190,000 The followin g AFE's were closed to field charges during July: AFE No. Title Authorized 9639 9719 9590 9521 Revisions to Emission Recovery System Aberdeen PVC Resin Expansion Critical Spare Equipment New VCM Rai1 spur $100,000 850,000 59,000 11,000 A completion report was issued for the following AFE: AFE No. Title Authorized 9751 Centrifugal Air Compressor Repair $ 45,000 Design Design work is in progress on the following projects: Resin Reclaim System Emergency AMS Kill System Modifications to Make Profile Dry Blend Compound Line III Debottlenecking Fire Protection Improvements - Phase III V-10 Centrate Heat Recovery Vinyl Initiator Charge Pots Reactor Seal Access Platform Slurry Delumper New Storage Track Plasticizer Irritant Control CenIrate Heat Recovery AFE Activity 1 . AFE 9729 ~ Fire Protection Improvements - Phase III - M. Ingle & J. P. McKee Construction of the pump house is complete. The jockey pump has been installed. Piping and electrical are 95% complete. DTH 000021759 MECHANICAL ENGINEERING - (Cont.) AFE Activity - (Cont.) 2. AFE 9570 ~ Replace T-101 P. A. Tank - J. P. Windham Drafting and purchasing is complete. Construction bids have been requested. 3- AFE 9600 - Calcium Stearate Addition System - M. S. Richards The storage tank and agitator are on order. Tie-ins are planned for the shut down in the new module. Electrical design is in progress. **. AFE 9630 ~ Water Stripping (Air) - M. Ingle & J. L. White This project is operational. Minor modifications are in progress. 5. AFE 968O - Fixed Point Monitor Data Computer and Warning Lights - R. B. Harned Construction is progress. There was a delay in shipment of the computer from Ponca City. The delay should not affect project completion. 6. AFE 9710 ~ Fire Protection Improvements - Phase III - J. B. Elkins & W. J. Modica Engineering is approximately 70% complete and drafting is 50% complete. 7. AFE 9730 ~ Compound Line III Debottlenecking - J. J. Tomek Structural design is in progress. Request for quotes were sent out for all major equipment. Planning data is being prepared to evaluate the alternate silo locations. 8. AFE 9760 - Emergency AMS Kill System - J. L. White Piping drawings for the new reactor area are being checked. Instrumentation drafting is in progress. 9. AFE 9770 ~ Reactor Pressure Relief Modifications - J. L. White All material has been been received. Installation of relief valves and reactor studding out 1ets are scheduled for August. 10. AFE 9790 ~ Resin Reclaim System - P. H. Meiers & M. S. Richards Design is approximately 50% complete. Piping approval drawing are read for review and comments. Equipment purchasing is proceeding. 11. AFE 9800 - Plasticizer Irritant Control (Air) - R. Milner & R. B. Harned Design work is complete for installation of the pond aerators. Bid packages have been prepared and bids are due in August. DTH 000021760 MECHANICAL ENGINEERING - (Cont.) 12. AFE 9531 ~ Vinyl Initiator Charge Pots - S. Jones & J. P. Mckee Piping drawings are being revised per approval comments. Instrumentation engineering is 50% complete and drafting has just begun. 13- AFE 95^1 - VCM Tank Farm Modifications - R. B. Harned The contract has been let for the mechanical installation. The electrical and instrumentation bid packages have been issued and bids are due in August. Piping tie-ins will be installed during the august shutdown. AFE 80-895 - Interplant Communication - Phase II - R. B. Harned The Gaitronics stations have been received. The installation of conduit for the additional stations is nearly complete. 15- AFE 9551 - V-10 Centrate Heat Recovery (Energy) - S. Jones & J. P. Mckee Foundation drawings are complete and mechanical drawings are being checked. Instrumentation engineering is 1*5% complete and electrical engineering is 25% complete. 16. AFE 9561 - Cooling Tower Fan Controls - R. B. Harned Specifications for control sequences and thermowells were finalized. Control units are scheduled to ship in August. 17- AFE 9581 - Dryer Building Ventilation - J. P. Windham Installation of the fans in the dryer buildings is in progress. Electrical installation is scheduled for early August. 18. AFE 9591 ~ Sifter Overflow Reclaim System - J. P. Windham & R. E. Milner The control system design has been revised and completed. Equipment specifi cations are being prepared. Purchasing of instrumentation is in progress. 19- AFE 96*41 - Slurry Delumper - M. S. Richards The mechanical design is 65% complete. The electrical design is in progress. The piping tie-in will be installed during the August shut down. 20. AFE 9671 " New VCM Rail spur - Herzog-Hart & J. A. Dixon The constract was let in July. Construction is scheduled for August and September. Completion is scheduled for the first week in October. DTH 000021761 MECHANICAL ENGINEERING - (Cont.) Construct ion - G. A. Morgan The following projects were completed in July: 1. No. 2 Pond Bypass. 2. Fire Protection Jockey Pump 3. Demolition work - Batch Water Stripping k. Curbing of Fire Training Ground and Plasticizer Tank Farm Fuel Storage Areas. 5. Air Conditioning of Warehouse Ladies Rest Room. 6. Noise Abatement Projects 7- V--11 Dryer Building Walkways 8. Clean out of API Separator 9. Painting of 281-677 Silo Walkway 10. Miscellaneous roof leaks 11. Breathing Air Modifications The following contracts were issued during July: l. New VCM Rai1 spur 2. NPD No. 2 Pond Bypass 3. Revise Main Restroom Ventilation k. Installation of Piping, Equipment and Structural for VCM Tank Farm Revisions. 5. Installation of Relief Valves, Piping and Structural for New Module Relief Valve Modifications. Forty register tickets were issued during July. DTH 000021762 ABERDEEN AUTHORIZATIONS REPORT (?) Thru July, 1981 AUTH. CAPITAL NO. DESCRIPTION DATE AUTH. APPROVED AFE AMT. (1) EXPENDEO TO DATE (2) COMMITTED TO 0ATE FINAL TOTAL EST. COST COMP. UNDER (OVER) AUTH. AMT. EST. EST. COMP . CL0S. DATE DATE REMARKS 9609 9629 9639 9689 Reactor Inert Vent System Air Compressor Revisions to Emission Recovery Sys. Diking of Sphere & Curbing of Drum Storage Areas 6/28/79 7/9/79 7/12/79 9/15/79 90.000 340,000 100,000 170,000 14.541 302,079 80,260 137,578 14,541 307,808 96.849 159,078 90,000 308.000 100,000 170,000 0 32,000 0 0 12/81 3/82 6/81 9/81 7/81 10/81 9/81 12/81 Project on hold. Closed to field charges. Closed to field charges. Revisions in progress. 9699 9709 9719 9729 9759 9530 9550 9560 9570 9590 9600 9630 9660 9670 9680 9690 9700 9710 Plant Oryer Debottlenecking 9/15/79 Facilities for Multiple Grade Resin 9/20/79 80,000 870,000 Aberdeen PVC Resin Expansion 9/10/79 850,000 Fire Protection Improvements Phase 11 10/1/79 490,000 Aberdeen PVC Resin Expansion Spare Incinerator 12/10/79 11 ,150,000 1/23/80 650,000 P.A. Handling Improvements 3/3/80 63.000 Safety Equipment 3/12/80 25,000 Replace T-101 P.A. Tank 3/27/80 119,000 Critical Spare Equipment 3/26/80 59,000 Calcium Stearate Addition System 4/2/80 84,000 Water Stripping 4/30/80 810,000 Hot Water Charge Tank Replacement 6/4/80 160,000 Laboratory Equipment 7/9/80 32,000 Fixed Point Monitor Data Computer and Warning Lights 9/4/80 113,000 8reathing Air Modification 9/9/80 21,000 Compound Fines & Streamers Removal 10/1/80 95,000 Fire Protection - Phase ill 10/14/80 385,000 47,670 496,690 887,200 353,624 74,950 660,625 887,200 381,828 6,737,800 9,542,300 394,203 450,225 32,470 32,574 26,575 29,288 64,699 70,590 11,431 60,406 12,929 18,726 382,294 389,261 141,632 141,948 30,334 31,034 40,870 79,870 9,394 0 1,707 15,144 29,524 1,707 80,000 725,000 887,200 490,000 10,450,000 550,000 63,000 29,288 119,000 60,406 84,000 510,000 160,000 31,034 113,000 21,000 95,000 385.000 0 12/81 3/82 145,000 12/81 3/82 (37,200) 7/81 10/81 0 9/81 12/81 Construction In progress. Construction in progress. Closed to field charges. Construction in progress. 700,000 12/81 3/82 100,000 10/81 1/82 0 12/81 3/82 ( 4,288) 5/81 8/81 0 12/81 3/82 ( 1,406) 7/81 10/81 0 12/81 3/82 300,000 10/81 1/82 0 6/81 9/81 966 12/80 9/81 0 9/81 12/81 Construction in progress. Construction in progress. Engineering In progress. Closed to field charges. Bids requested. Closed to field charges. Engineering in progress. Revisions in progress. Closed to field charges. Closed to field charges. Construction in progress. 0 8/81 11/81 Project operationaT. 0 10/81 1/82 Engineering scheduled. 0 10/81 1/82 Engineering in progress CED. 9720 9730 Reactor Agitator Replacement Compound Line III Debottlenecking 10/14/80 420,000 10/16/80 1 ,350,000 9740 Modifications to Make Profile Dry Blend 10/27/80 200,000 9750 Rotary Dryer Insulation (Energy) 11/10/80 22,000 9760 Emergency AMS Kill System 11/15/80 335,000 9770 Reactor Pressure Relief Mod. 11/25/80 560,000 9780 Centrate Heat Recovery 12/8/80 300,000 9790 9800 Resin Reclaim System Plasticizer Irritant Control (Air) 12/14/80 12/15/80 727,000 80,000 9810 Replacement Gearbox for Farrel Mixer 12/18/80 . 73,000 9511 9521 9531 9541 Miscellaneous Projects Under $10,000 1/9/81 New VCM Rail spur 1/30/81 Vinyl Initiator Charge Pots 1/21/81 VCM Tank Farm Modifications 1/21/81 170,000 11,000 165,000 90,000 80-895 Interplant Communication-Phase II 1/22/81 55,000 9551 V-10 Centrate Heat Recovery (Energy) 2/17/81 125,000 9561 Cooling Tower Fan Controls (Energy) 2/17/81 40,000 9581 Dryer Building Ventilation 3/20/81 23,000 9591 Sifter Overflow Reclaim System 3/20/81 200,000 9601 Compliance with EPA VCM Standard (Air) 3/25/81 72,000 9611 Recovery System Revisions 3/25/81 30,000 9621 Laboratory Equipment 3/25/81 42,000 9631 9641 Ground Water Monitoring (Solid) Slurry Delumper 3/24/81 5/14/81 30,000 35,000 9651 9661 Safety Equipment Waste Water Treatment Rev. (Water) 6/8/81 , 6/19/81 106,000 560,000 9671 9681 New VCM Ra i 1 spur 6/30/81 Miscellaneous Projects Under $10,000 7/31/81 194,000 145,000 9691 9701 Reactor Agitator Two Speed Motors Misc. Energy Savings ProJ. Under $10,000 7/2/81 7/13/81 40,000 25,000 9711 Plasticizer Spill Containment 7/27/81 42,000 9721 Emergency Cooling for Reactors 7/30/81 190,000 191,623 17 16,969 191,753 69,517 55,460 420,000 1,350,000 200,000 20,000 66,996 98,333 23,967 123,133 28,557 0 115,798 17,612 5,534 26,676 0 7,641 0 1,101 0 0 27,391 94,367 338,849 61,528 234,610 31,810 69,400 187,820 17,612 39,505 49,154 31,755 23,739 19,840 15,149 14,877 12,434 27,391 335,000 460,000 300,000 727,000 80,000 73,000 170,000 17,612 165,000 90,000 55,000 125,000 40,000 23,000 200,000 72,000 7,415 31,400 467 0 0 0 0 0 0 0 14,110 38,516 17,071 20,746 0 0 189,512 2.478 0 0 30,000 42,000 30,000 35,000 106,000 560,000 194,000 145,000 40,000 25,000 0 0 42,000 0 0 190,000 0 10/81 1/82 Agitators received 0 6/82 9/82 FCM barrel to ship 10/81. 0 10/81 1/82 Engineering in progress. ( 5,391) 8/81 11/81 0 10/81 1/82 100,000 12/81 3/82 0 3/82 6/82 0 3/82 6/82 0 9/81 12/81 0 10/81 12/81 0 12/31 2/82 ( 6,612) 7/81 10/81 0 11/81 2/82 0 1/82 4/82 0 9/81 12/81 0 5/82 8/82 0 11/81 2/82 0 9/81 12/81 0 3/82 6/82 0 12/81 3/82 803 complete. Engineering in progress. Construction in progress. Engineering In progres.. Engineering in progress; CED Engineering in progress. Gearbox to ship 10/81. Sixty-two projects approved. Closed to field charges. Engineering in progress; CED Construction in progress. Revisions In progress. Engineering in progress; CED Equipment on order. Construction in progress. Engineering in progress. Engineering in progress. 0 12/81 3/82 Revisions in progress. 0 8/81 11/81 Equipment on order. 0 10/81 1/82 Contract let. 0 2/82 5/82 Engineering in progress. 0 6/82 9/82 Engineering scheduled. 0 9/82 12/82 Engineering scheduled. 0 12/81 3/82 Construction in progress. 0 12/81 3/82 Five projects approved. 0 4/82 7/82 Updated quotes requested. 0 12/81 3/82 Engineering scheduled. 0 1/82 4/82 Engineering scheduled. 0 4/82 7/82 Engineering scheduled. EXPENSE 9020 Repairs to Line 1 Compounder 11/24/80 38,000 0 0 38,000 0 11/81 2/82 Parts ordered in January. DTH 000021763 PERSONNEL - R. A. HILLER EMPLOYMENT Romona Faulkner - Steno Clerk TO/FROM LEAVE OF ABSENCE None. TRANSFER/PROMOTION John Sutton transferred from the Compound Department as a Compound Operator to the Warehouse Department as a Warehouse Worker "B". Bernard Garth transferred from the Service Warehouse Department to Trans portation Warehouse. RETIREMENT None. TERMINATION Frank Brewer, Casual Labor Cleveland Brown, Jr., Casual Labor David Volz, Casual Labor OTHER During July there were 15 casual labor employees on payroll. Total hours worked were 2583.75. DTH 000021764 CONOCO CHEMICALS Aberdeen, Mississippi July 1981 MONTHLY PERSONNEL REPORT Salaried Employees 87 Minority Employees # Hourly Employees 161 Salaried 6 n Total Employees Employees (Hourly) 248* Hourly Total 59 m 65 26 New Employees Terminations Hourly Min. Hired % Min. Hired Hourly Min. Term. % Min. Term. DEPARTMENTS PAR # EMPLOYEES min. emp: . % MIN. NEW HIRES YTD TERM. YTD TURNOVER YTD Warehouse 11 9 ' 1 11 0 0 00 0 0 Gen. Plant Maintenance 11 52 13 48 5 38% 0 10 0 0 0 0 8 17% 0 0 0 | 5wV 0 0 Laboratory Compound 22 37 20 35 4 20% 0 0 0 0 0 0 26 74% 0 0 0 0 0 0 Vinyl Plasticizer - 40 4 32 4 13 b0% 0 0 0 0 0 0 2 50% 0 0 0 -0 0 0 Number of Applicants: Month 0 Year to Date 103 APPLICANT BREAKDOWN: # Minority ^ Female 0 0 % Minority % Female 0 0 , 'Includes eight (8) temporary employees. **lncludes one (1) retirement. Retirements are not included in turnover rates. Hires (Hourly) : Month a Year to Date Terminations (Hourly) : 10 Month 0 Year to Date 1 *' Overall Turnover 0 Projected Annual Turnover _____ 0 DTH 000021765 4) 10 o Loi i m 0) W^ ia u> w ^n w <k> ca cr\ O -a- <r**->* ca <K> d-P ** O <rK^>. o<*o? -a- -r d-p cnj <h> -- o oo d-e ca to t-- O &$ <0 (ft o 03 43 o tA c eft 43 43 eft c -Q <u to o cdP o o *? o oo &?&$&? dP oo o o la o o o o 0 a\ rsJtOCg-3-COOOOCO tA -- CA OO LA -- CO Xto CO cn >* 3 cc LlJ > o L. 1_ 43 4-1 > to oo vO *3" -- CO LAAJ H Jal 0i-3 t3- 4-* O to X LrA*>LA rgOLAtAcMO orL,*A .iOAPvLA.rLsA 03 vD N \C<A Cr-O* r.--- to CAr-. oo oo CT3 Lr-A. (N aO- -3* LA LA vO r-. AJ O vO oo -a* CN 41 O >* 4) C 4->eft 03 o 3 o C 43 03 01 4) C 0 CL a4) 01 3 <D X .o 01 41 3 O X 01 c 43 o 03 N CO Q_ U >* (ft C 03 >K 03 (ft c o eft c o <0 l_ a> m a. L. o 43 O. c o c >. <0 *o > <0 *o (ft X 0> (ft 4) c o 03 (ft C L- o 5 *o c (0 > <0 *o 03 c 0 -C 1_ 0 01 3 c *o oc 0) (ft t_ >. o3 01 "O L- O 03 3 01 03 0) C Uo 0c3 (ft L. 3 O L. o 2 01 O 3 Oi 4) 4) 3 o 03 01 C E L. o 4) 5 > O0 03 c TJ 3 o 4X3 DTH 000021766 PROCESS ENGINEERING - R. A. Frohreich A. Expans ion Work is continuing in all areas of this project. Tie-ins in the new module reactor area will be made during the scheduled shutdown of the area in early August. Also utility tie-ins will be made at this time. A meeting was held with PED to review the initial issue of the Fluid Bed Dryer oper ating manual. The plant is preparing the operating procedures for the other areas. Change orders for spare cooling water supply pumps, a deaerator for the boilers, a boiler feedwater pump, a spare rotating assembly for the centrifuges, an additional product silo, and a reactor seal access platform were approved. Engineering on these projects will begin in August. B. Emergency Reactor Cooling System The class "A" design to provide emergency cooling and backup instrument air was issued and the AFE request for the project was submitted. C. Dryer Area Vacuum Clean-Up System The class "A" process design to provide a vacuum cleaning system for the dryer areas is being prepared. D. Reactor Venting Problem Work has began to determine the composition and source of the inerts which build up in the reactors during polymerization. E. Normal Kill Solution Addition System The class "A" design to provide mixing, storage, and metering the normal kill solution was issued. This design consists of a tank, a drum pump, a transfer pump, a filter, and piping to the reactor injection pots in both reactor modules. F. 10-8 Plasticizer Production The class "A" design to provide 10-8 alcohol and 10-8 plasticizer storage and transfer facilities is being prepared. G. Glycerin Make-Up System The class "A" design to revise the glycerin make up system is being prepared. H. Dryer Optimization Study Several tests were conducted on rotary dryer number 1 in which drying air flow rates were reduced. Preliminary results indicate that energy savings may be realized without adversely affecting dryer resin rates. Further tests will be conducted toassure that drying rates are not reduced at the lower air rates. DTH 000021767 PROCESS ENGINEERING (Cont.) I. Batch Water Strippers Process engineering continued to provide support for the operation of the batch water strippers. A process design to install an automatic flush for the new module transfer, 1ine was issued. J. 1982 Capital Budget Work continued on preparation of the 1982 Capital Budget. The second issue of the budget was issued. DTH 000021768 ENVIRONMENTAL - V. E. Messick Particulates Two dryer exhausts were sampled for particulates and were within allowable 1imit s . Water All parameters were within NPDES limitations in July. The quarterly NPDES discharge monitoring report was submitted to the state of Mississippi. The API separator was cleaned out in July. The material removed from the API was placed in drums and prepared for disposal at Chemical Waste Management. VCM The compliance test for the batch water strippers was conducted on July 2$. Stripping results were well below the 10 ppm VCM process waste water limit. test report is being prepared. The Hazardous Waste Management A total of 320 drums of hazardous waste were shipped to Chemical Waste Manage ment's Alabama site for disposal. Manifests have been received for two of the four shipments. DTH 000021769 Flow GPM Jan. _ Ave. 1069 Max. 1297 Feb. - Ave. Max. 757 819 Mar. - Ave. Max. 753 790 Apr. - Ave. 946 Max. 1200 May Ave." 846 Max. 1200 June _ Ave. Max. ' July Ave. Max. 739 917 746 922 Aug. Ave. Max. Sept. - Ave. Max. Oct. Ave. Max. Nov. _ Ave. Max. Dec. Ave. Max. NPDES Ave. Max. . - TABLE I -WATER COMPLIANCE WITH NPDES PERMIT PARAMETERS BOD PPM LB./DY. 39 504 57 887 COD PPM LB./DY. 69 888 106 1650 Sus. Solids PPM LB./DY. 7 93 9 114 Diss 02 11 95 , 43 382 18 154 . 56 479 10 90 11 103 36 330 51 466 10 118 20 253 31 360 41 519 12 125 14 163 43 470 54 629 20 I83 34 314 12 107 16 130 56 502 79 729 39 339 53 420 7 65 8.9-9.8 10 86 11 93 8.3-8.9 17 139 13 151 8.2-8.9 19 240 13 138 7.4-8.4 17 198 - 18 157 6.2-8.2 27 249 22 190 28 209 6.2-7.5 32 431 43 800 _ 1462 - 2713 _ 674 - 1396 6.0 -=r 0 1 LTV OO ph 7.4-7.8 7.5-7-9 7.6-7.7 6.9-8.1 7.3-8.0 7.6-7-9 7.7-8.0 6.0-8.5 DTH 000021770 ENERGY CONSERVATION J. F. Perez-Velasco I. Plant Operations Total energy consumption for July was 10^4.037 MMM BTU's. The energy consumption per pound of product increased to 3188 BTU/lb. as compared with 3088 BTU/lb. for June. I I. Plant Energy Conservation Program Steam Leaks Twenty-one (21) steam leaks were repaired in July. Boiler Boiler #1 and #3 were shut down for repairs during July. Opportunity was taken at that time to acid clean the tubes and make visual check of boiler #3 economizer. Energy Reporting Second quarter report was prepared during July. A CMA adjusted energy savings of 38.8% was obtained for the three month period versus 1972 equivalent energy usage. DTH 000021771 ITEM Control Period Production, MM Lbs. Resin Dry Blend Compound Plasticizer TOTAL Natural Gas Consumption, MSCF Conversion, BTU/SCF Energy Consumption, MMM BTU Electricity Consumption, MM KWH Conversion, BTU/KWH Energy Consumption, MMM BTU Propane Consumption, M Gal. Conversion, BTU/Gal. Energy Consumption, MMM BTU Total Energy Consumption, MMM BTU Energy Consumption , BTU/Lb. Boiler Operating Data No. 1 No. 2 No. 3 ENERGY CONSERVATION DATA 1981 July 23.4 3.8 4.5 0.9 32.6 49354 1020 50.341 5.3696 10000 53.696 0 .92000 0 Avg. Stack Temp. 1981 360 367 328 415 293 413 O CO CP 104.037 3188 Avg. % Excess Air 1981 1980 52 25 31 27 38 23 1980 July 17.0 2.2 3.4 0.9 23.5 33298 1020 33-964 4.2555 10000 42.555 0 92000 0 76.519 3256 DTH 000021772 LABORATORY - R. D. Jackson CUSTOMER COMPLAINTS Customer Products Complaint Report By L. B. Plastics, Inc. 80273G Wet Dry Blend RDJ WAIVERS Date Identification Product Customer Reason 7-6 7-7 7-20 7-20 7-24 7-24 7-28 7-28 7-29 CONX 45258 CONX 45755 PLCX 43707 CONX 45713 CONX 45797 CONX 45768 PTLX 41835 CONX 45718 T2 8ll 80273G 5385-3 5385-3 5385-3 80273G 80273G 5385-3 5385-3 5305 Kebco World of Plastics World of Plastics Charlotte Pipe Northern Waterworks Kebco World of Plastics Charlotte Pipe Celanese Pipe Equi librium Torque Particle Size Bulk Density Particle Size Equilibrium Torque Equi1ibriurn Torque Particle Size Particle Size Viscosity PRODUCT SERVICE & DEVELOPMENT CJM RDJ ELK ELK CJM CJM ELK ELK RDJ Sample Shipments Ship Date Product Amount (Lbs.) 7-1 7-1 7-1 7-2 7-3 7-8 7-10 7-14 7-14 7-17 1-11 7-28 7-29 7-30 7-31 7-31 7-31 16851 CL BL 50 25 5425-0G 20 35851 Nat. 50 5385 10 5385-1 10 5425 10 5465 10 38631 Nat. 50 34711 Grey 100 38551 Nat. 100 16851 CL BL 50 100 5305-1 4,500 RP 100 DB 20 5305 2,000 5385-1 10 80273G DB 220 5425 0G ' 4,500 5385-3 150 16851 CL BL 50 50 Customer Americhem Inc. Ca r1 on Interstate Wire Corp. Conoco, Ponca City Stauffer Chemical Co. Requested By KJQ NBB KJQ RBM DLG Taylor Cable Co. Atco-Flex Inc. Taylor Cable Co. Advanved Plastic Corp. Conoco , Ponca City Jim Walter Research Corp. Conoco, Ponca City Fritz Airfreight Mitsui & Co. Inc. Bristol Products Petrolite Corp. Therma Tru MFM JFN MFM MFM COEDS CJM COEDS JPM COEDS COEDS COEDS DD DTH 000021773 LABORATORY - (continued) COMPOUND DEVELOPMENT AND SERVICE Special Compound Testing Specification tests were run on five (5) production lots of Western Electric compounds - 1 lot each of 3^861 Gray 546, 34862 Gray 546, and 36862 Natural and 2 lots of 36861 Natural. Plasticizer content and flammability were tested on eleven (11) shipment samples. Testing is partially complete on the first production lots of 48651 and 48961 for Bel den. Compound Property Verification Property testing is complete on twenty (20) active compounds. Dry Blend Development Quality control standards were prepared for 80174, 80273G and 90171 dry blends. QUALITY CONTROL TESTING Resin Regular Samples = 442 Bag Samples = 41 Other In-Process Samples = 3092 Bulk Shipment = 181 (Railcars = 99; Trucks 82) Dry Blend Blenders Produced = 410 Blenders Tested = 408 Blenders Adjusted = 17.8* Other In-Process Samples = 558 Bulk Shipments = 36 (Railcars 15; Trucks 21) Compound Blenders Produced = 720 Blenders Adjusted = 2.5% Line 5 Production = 33 skids Other In-Process Samples = 223 Bulk Shipments = 16 (Ra i 1 ca rs 13; Trucks 3) DTH 000021774 LABORATORY - (continued) QUALITY CONTROL TESTING (continued) Resin Heat Stabi1 i ty Oven heat stability tests were run on fifty-eight (58) blends of resin. All the samples were acceptable, and 5305 and 5465 resins continue to average a little better stability than 5385 and 5425. Raw Material Testing Eighty (80) lots of plant raw materials were tested and accepted. Several lots of Ongard 2 flame retardent would have been rejected for poor dispersion if the supplier had been able to supply better materials. They insist that better dispersing Ongard 2 will be available soon. Two samples of Halthal EP lead stabilizer have been tested and compared with Cyastab 988 and Dythal XL. The Halthal EP disperses easily but does not stabilize quite as well as Cyastab 988 or Dythal XL. Americhem 2013"T1 gray color concentrate has been tested and approved as a substitute for Wilson 32-GY-18 in making Western Electric 34861 Gray 546. Americhem 1943-T2 gray color concentrate was tested and approved as a sub stitute for Wilson 32-GY-16 gray. We are replacing Wilson products with other materials due to Wilson's deteriorating quality and poor response to our complaints. RVCM of Shipment Samples The following shipment samples were tested. Product # Samples Average RVCM, ppm 5305 5385 5425 5465 Dry Blend 120 48 15 3 11 1,1 0.4 0.1 0.1 0.4 MISCELLANEOUS PROJECTS Volume Resistivity Testing Samples of 5425 and 5465 resin were tested for volume resistivity (VR) and all values were good. Twenty-seven (27) specimens from Ponca City were tested for VR and reported. Their resistance testing equipment was out for repair. DTH 000021775 LABORATORY - (continued) MISCELLANEOUS PROJECTS - (continued) RVCM Of In Process Samples The following in process samples were tested for residual vinyl chloride (RVCM). Sample Type # Samples Average 1 Reactor slurrys Batch Water Stripper 5305 Drier Sarnples 624 47 124 165 6.4 2.2 None of the reactor daily averages exceeded 400 ppm. Viscosity A total of 751 dilute solution viscosity measurements were made on resin in July. Spec! al A total of 110 special samples were tested in July. Most of these were the waste water samples for COD analysis. Dosimet ry A total of 111 personal dosimetry samples were tested for VCM content in July. Computer New programs were prepared for the lab computer to permit L S N particle size data to be entered and stored implace of screen data. DTH 000021776 TRANSPORTATION - J. E. Stark Shipment By Product - M Lbs. Res i n PIasticizer Dry Blend Compound TOTAL Jul y 15,617 76 3,220 3,557 22,470 Year to Date 137,754 672 27,092 27,111 192,629 Number of Shipments by Mode R/C O.T. Bulk O.T. Van C.O.T. C.C. TOFC CPU TOTAL Resin - Bulk 77 49 126 - Package 7 2 9 18 - Export 8 35 43 PI asticizer 22 Dry Blend - Bulk - Package - Export 18 7 3 Compound - Bulk - Package TOTAL 9 To? 3 28 ~To "80 Backhauls for July 27 Number of Shipments by Month - Year to Date 0 21 39 7 3 12 5 15 48 7 IT T7 ~23$ 3 30 R/C Bulk Var. C.O.T. C.C. TOFC CPU Tota 1 January February March April May June July 91 48 200 91 55 172 132 65 208 96 38 181 111 49 120 123 55 104 60 74 80 2 91 0 40 6 54 0 11 03 05 07 0 55 487 0 58 416 0 74 539 0 69 395 0 68 351 0 50 307 0 47 298 Material Handling Report Packaged Resin from Production Packaged Compound, Dry Blend from Prod. Transferred from Main to Prairie Transferred from Prairie to Prairie Reverse Transfer Resin to Plant Reverse Transfer Cmpd. to Plant Shipment from Warehouses Special Packaging Transferred from Prairie to Main TOTAL M/Lbs. 2,228 3,119 2,349 81 810 243 1,903 1,539 1,580 13,851 T/L 55 77 58 2 20 6 47 38 39 3W DTH 00002177l TRANSPORTATI ON - (continued) Off-Grade In Storage Material Sifter Overflow Resin "BC" Resin "H" Mi 1 1 Scraps Compound "B" Compound "H" Dry Blend "O.G." TOTAL M/Lbs. 598 3,^87 5 kk 7k 1,28k 16 602 S"505 T/L 15 86 13 2 32 0 15 TSJ DTH 000021778 LOCATION MAIN-East TOTAL M SQ. FT. 48 Prairie 12-1 12 12-2 12-3 22 21 12-4 12-5 22 21 12-6 21 12-7 12-8 12-9 12-12 21 21 21 21 Total 251 _ CONOCO TRANSPORTATION . ...July 31. 1981 ABERDEEN WAREHOUSE CONTENTS ESTIMATED MM POUND ON FLOOR OPEN TO Compounds 6. 0 Dry Blend .3 Export Resin .4 Conoco Resin HDPE Dry Blend Conoco Resin .4 .1 2. 4 ____k.7. 3.3 10.0 ....... 5. :ii.,o 2.4 i .i 1.5 3.5 Conoco .3 Export Resin .8 1 . 1 2 .4 3.5 Conoco Resin Resin O.G. 4. 4 *' 4* A * 3.5 Mill Scraps .1 Cmpd O.G. .8 Dry Blend O.G. .5 Sifter Overflow .3 Resin O.G. Compound .2 .1 1.9 .6 2.5 ro 00 Resin Raw Material .2 3.1 . 4 3.5 Resin O.G. 3. 3 3.3 . 2 3.5 Conoco Resin 4. 0 * 4.0 3.5 Conoco Resin .6 . 6 2 . 9 3.5 Dry Blend O.G. .1 S.O. .. 3 Comp. O.G. Mill Scarp Sub-Total (Plug-Aisles) Total Conoco .4 _____ u-L DTH 000021779 . 9 2 . 6 3.5 * 42,0 28 . 9 14 5 1. 4 43. 4 MED I CAL CASES 8 ABERDEEN CHEMICAL PLANT INJURY PERFORMANCE 6 b 2 0 40 30 20 10 0 REQUENCY = TOTAL INJURIES (FA OR MC) X 12 TOTAL EMPLOYEES DTH 000021780 MONTHLY HOURLY TURNOVER 10 9 8 7 6 5 4 3 2 1 DTH 000021781 ENERGY USAGE Monthly 12 Month Moving Average DTH 000021782 MM POUNDS ABERDEEN PLANT PRODUCTION MM POUNDS 60 50 40 30 20 10 40 35 30 25 20 15 10 5 I 25 20 15 10 5 ----------- ACTUAL ----------- CUMULATIVE DTH 000021783 ABERDEEN PLANT QUALITY PERFORMANCE STANDARD 1.35 v. DTH 000021784 ABERDEEN PLANT EFFICIENCY 1981 STANDARD 1.01936 0 1.020 1.010 1.000 STANDARD 1.01300 STANDARD 1.00580 1.250 j)l-200 1.150 1.100 1.050 ) j'EEEE 1",.ii -------------- -------------------- --------------------- 1 .... .,. ---------------- -t-------------------- -P-------- RAW TALrCONSUMPTj ION --------------- 1--------------- 1---------_-------- j--------------------- , -- ______ ------------------- f-------------- --i-------------------1_______ _____ 1__________ J --I--------------- 1-------------------- {--------------- ---- 1 1--7 I ---------------------------- --------------------- _ i__ ------------------- j '-------------------- 1-------------------- 1-------------------------------- ---------- ---------------- S\1 /- ----- --- /----- 1 "5____ ------- -------------1 v r, : _____ ____ 1_____________ ______________ 1_______ 1 ... "I . ------------- ------- {------------------- --------------- -- --, r ---- -------------------- r. ----------- ------ ^...... - ' -t................... mm --------- , . 1 L J T------.-..--- . .; ^--------------------- \! 1~ . ___i____ ________ -- -------------- --------------------------- -- ------------------ 4 ' 1 ... - .\---------- ~ * ... ------- ----------- - 1--------..-,;:-_-_--_-_--_-_-----------' 41--" ---.-.-.-..-. + -- *-41 ' - --- - T -- -t" : -.1 JAHUAftV Ni*CM Mir . 1. 4 -------- -- i_____ r: * JUNE J'JIA 1 AUGUST SfniMPfr | OCICBit ______________ 1_____________ i 1 9 Ai_ -- -- -- -------------------- - NOVEMBER OCCFMlR STANDARD 1.10500 MONTHLY CUMULATIVE 000021785 dth ABERDEEN PLANT INVENTORIES 4.0-: 3.0. 2.0 1.0- 0- B } DTH 000021786