Document rBV83Zv4XEX82z0ajg2E9EZoV

SAFETY - A. H. Sather OCCUPATIONAL INJURIES Injuries Treated April 1980 Year-to-Date 1979 Year-to-Date First Aid Medical Cases "Restricted Workday Cases Restricted Workdays Lost Time 2 18 19 01 03 00 8 1 2 24 0 Injuries by Department Vinyl Operations Compound Operations Maintenance Laboratory Receiving and Warehouse Office 06 07 3 13 02 00 00 5 0 4 0 0 2 Injuries by Type Cuts and Abrasions Eye Injuries Burns Bruises Strains and Sprains Other 2 13 13 02 16 04 00 2 3 2 4 3 0 The medical case occurred to a General Mechanic "A" who was using a ratchet wrench and torque multiplier to tighten the stud bolts on the condenser lid of 744 reactor. The torque multiplier handle slipped off of the condenser rinse nozzle flange causing him to pinch his fourth right finger tip between the ratchet wrench handle and a stud. As of April 30, 1980, the plant operated 300 days or 387,939 manhours without a disabling injury. SAFETY RULE BOOK The Aberdeen Plant Safety rules were rewritten during the reporting period. The final copy of this was taken to the printer in early May. Issue of the rules to all plant personnel is targeted for the week of May 12, 1980. FIRE SCHOOL Mickey P. Blackwell, Vinyl Operations Engineer, attended the Lamar University Fire School April 28 through May 2, 1980. -1DTH 000019258 SAFETY - (continued) NEW EMPLOYEE ORIENTATION During the reporting period two new engineers received Safety Orientation Skeeter Reed, Process Engineer and Don White, Mechanical Engineer. EMPLOYEE SAFETY RESPONSIBILITIES PROGRAM The revisions requested as a result of previous comments to Part 1 were made, reviewed and comments again forwarded to M. S. Reynolds, Employee CommunicationsHouston during the reporting period. EMERGENCY PLAN The Plant Emergency Plan was revised and reissued to all holders of the PVC Plant Safety and Health Manual. SAFETY MEETINGS Topics covered in all Plant Safety Meetings included the following: 1) Lockouts - the film "Lockout for Safety" was shown and the Plant Lockout Procedure reviewed. 2) Live Electrical Parts - The emphasis centered upon keeping live electrical parts properly covered and. authority limitations re garding access to live parts in motor starter enclosures. 3) Emergency Plan - This consisted of a review of the revised plan as noted above. 4) Railcar Safety - Several injuries occurred in the plant in recent months which involved access ladders on bulk hopper cars. The rules regarding proper usage of these ladders were reviewed. OSHA COMPLIANCE Specific activity regarding OSHA Compliance was limited to personnel monitoring for VCM and Lead . A digest of this information is shown below. Also, the 744 reactor condenser flange faces were machined to improve the seal. This activity should reduce the likelihood of exposure to VCM vapor to employees working in this area. VCM - A total of 45 samples were taken for the reporting period, none of which indicated overexposure. Range (ppm) 0.0-0.5 0.5-1.0 1.0-5.0 5.0+ Number 44 1 0 0 45 Percent 97.78 2.22 0.0 0.0 100.00 DTH 000019259 SAFETY - (continued) Lead Greater than PEL* Less than PEL Number 0 17 17 * Permissible Exposure Limit -3DTH 000019260 VINYL - C. R. Miller Production Month Y.T.D. Budget 1. Total Production, MM Pounds 2. Production Rate, M Pounds/C.D. 3. Charges, Reactor Batches/C.D. 4. Total Charges 5. Reactor Stream Factor, % 6. Drying Rates, Average Pounds/Hr. 7. Dryers, Stream Factor, % 8. Accounting Days 20.7 690 16.3 489 72.5 5551 74.0 30 102.9 850 20.0 2398 83.7 5820 87.0 121 Vinyl department production for the month was 75% of budget at 20.7 MM pounds. Production levels were reduced as part of the inventory control program. The vinyl unit has undergone shutdowns in each of the reactor areas during April. These shutdowns utilized the inventory control downtime for new project tie-ins, mechanical repairs, leak repairs and the plant's annual inspection. Production rates for 5425 resin continues to be low with use of a single initiator system. Test runs using several initiator lots were conducted, but without favorable results. An alternate source for the initiator has supplied a test quantity to the plant for testing in May. Several test runs in addition to the 5425 initiator were also conducted in April. These included testing of a new suspending agent, J-40 methocel, and the drying and packaging of test quantities of pond resin. Resin Quality Summary Resin M. 5305 5385 5425 5465 Sifter Overflow Prime Pounds 1,446,206 11,793,161 6,464,614 348,700 "BC" Grade 40,450 570,550 38,250 "H" Grade 40,500 21,050 63,000 (123,765) % of Total Production 7.4 59.8 31.7 1.7 (0.6) TOTAL 20,052,681 649,250 785 100.0 Quality performance for the month of April was 96.9% customer grade with 3.2% "BC" grade and 0.01% "H" grade. The variable cost variance for the vinyl department was ($536.9 M) with ($687.8 M) due to price and $150.9 M due to efficiency. The variance due to product mix was $12.0 M. The only major price variance was ($620.0 M) for VCM. -4- DTH 000019261 VINYL - (continued) The only efficiency variance was $43.3 M for VCM.. The raw material require ment for the month was 1.00911 pounds VCM/pound of PVC versus a 1.01960 standard. (Y.T.D. is 1.01430) General 1. Resin bagging continued throughout the month due to low empty hopper car inventories. Resin bagging averaged 186 M pounds per day. 2. Approximately 340 M pounds of sifter overflow was rescreened during the month. -5DTH 000019262 COMPOUND - J. R. McCrimon Compound Production Month #1 s/Day Y.T.D. Line I, M Pounds Line V, M Pounds Line III, M Pounds Total, M Pounds Accounting Days 1,429 53 4,587 -- 207 2,757 92 9,861 4,186 139 14,655 30 121 Line I operated 27 days during April at an average rate of 53 M pounds per day. Major items affecting production efficiency were: Line V operation (69.5 hours), product changes (30 changes, 68.8 hours), dicers (34.9 hours), maintenance on plasticizer pump (6.7 hours), maintenance on blender bucket (6.1 hours) and quality control (5.7 hours). Line V operated 3 days during April. Additional tests on different screw configurations were conducted with Werner-Pfleiderer in the plant. None of the tests were successful. Line III operated 30 days during April at an average rate of 92 M pounds per day. Major items affecting Line III production efficiency were: product changes (9 changes, 47.5 hours), maintenance on B blender (17.3 hours), changing and cleaning FCM seals (10.9 hours), maintenance on FCM conveyor (8.7 hours), and maintenance on the Sweco star valve (6.5 hours). Quality performance for flexible compounds was 5.8% off-grade of which 56.4% was due to mill scrap. "BC" production was 0.5%. The raw material requirement for flexible compounds was 0.98936 pounds of raw material per pound of compound versus a 1.01299 standard. (Y.T.D. is 1.00914) The variable cost variance for compound was $73.4 M with $51.3 M due to price and $22.1 M due to efficiency. The variance due to product mix was ($14.7 M). The only major efficiency variance was $15.2 M for resin which reflects re blending of off-grade material from prior production. There were two major price variances for the month: $11.2 M for tribasic lead sulfate and $13.3 M for combined colors. Dry Blend Month #*s/Da.y Y.T.D. Production, M Pounds Accounting Days 1,763 84 6,631 30 121 Dry Blend operated 21 days during April at an average rate of 84 M pounds per day. Production included 80172 B, 80273 G, 80274 G, and 90171. Dry Blend production efficiency was affected by: No. 2 Wei ex motor out for repairs (116.0 hours), blender limited due to No. 2 Welex outage (39.0 hours), out of resin (22.2 hours), maintenance on the Orbitran (8.2 hours), quality control (10.2 hours) and inventory control (8.1 hours). -6- DTH 000019263 COMPOUND - (continued) Quality performance for the month was 99.99% customer grade. The raw material requirement for dry blend was 0.98995 pounds of raw material per pound of dry blend versus a standard of 1.00319. (Y.T.D. is 1.00949) The variable cost variance for dry blend was $7.1 M with $4.4 due to price and $2.7 due to efficiency. The variance due to mix was $19.4. There were no major price or efficiency variances. Plasticizer Month iTs/Day Y.T.D. Production, M Pounds Accounting Days 1,122 30 53 2,898 121 Plasticizer operated 21 days during April at an average rate of 53 M pounds per day. Production included: DIDP, 610P, and D0P. VRP production totaled 138 M pounds (12.3%). Production was limited by: R-4 inspection by MED and maintenance repairs (192 hours) and maintenance on level instruments in the phthalic anhydride charge system (12.0 hours). A new daily production record was set on 4/2/80 (133,548 lbs.). The raw material requirement for plasticizer was 1.11919 pounds of raw materials per pound of plasticizer versus a 1.10574 standard. (Y.T.D. is 1.14081) The variable cost for plasticizer was ($39.2 M) with ($40.0 M) due to price and $0.8 due to efficiency. Major price variances were: ($25.9 M) for ALF0L 610 and ($19.7 M) for phthalic anhydride. The only major efficiency variance for the month was $16.1 M for VRP which reflects reprocessing of recovered alcohols and oils into VRP. The variance due to product mix was ($6.4 M). General Total customer grade compound inventory increased to 5.2 MM pounds during April. Werner-Pfleiderer lab tests will be conducted in Ramsey, NJ during the week of May 19, 1980 and in Stuttgart West Germany, June 16-27, 1980. The purpose of these tests is to determine what modifications are required to the KP-800 to allow it to produce acceptable quality compound. Preblend will be produced and shipped in May for these tests. A Werner-Pfleiderer engineer from Germany will visit the plant May 20, 1980 to investigate problems with the pellet transfer system on Line V. -7- DTH 000019264 MECHANICAL - S. J. Vincent Vinyl There were three large reactor seal failures this period. Two of the seal failures were in the new module and one failure in the old module. The seal failures in the new module were a result of a mischarge in the 741 reactor causing major damage to the 741 reactor seal and a loss of seal oil flow to the 744 reactor seal resulting in its failure. The D-600 seal failed in the old module. This seal failed when the seal water flow was lost. There were no major reactor gearbox problems this month. Two large reactor condensors were brushed this month, both condensors were in the new module. The condensors cleaned were on the 741 and 742 reactors in the new module. The bottom gasket on the 744 reactor was replaced. The top condenser gasket surfaces on the large reactors were indicated and machined on the four new module reactor condensers. The repairs to the gasket surfaces were done to minimize and possibly eliminate VCM leakage from these areas. The motor on 742 reactor also had to be replaced because of bearing failure and water intrusion. This was the first large reactor motor in the new module to fail since startup of this unit. Reactors D-300, 744, and 743 were inspected by some MED inspectors. No evidence of chloride attack was found. The sections inspected were found to be mechanically sound. Reactor system valves replaced this month were the recovery and evacuation valves on the 744 condenser, kill bomb valves for D-600 and 741, D-300 main dump valve and the condenser cooling water valve, and the 743 steam stripping valve. The suction valve on the east VCM charge pump and the RVCM filter bypass valve in the old module were replaced. Repairs were made to the flexible conduit connectors on four reactors. The controls on the old module hot water tank were calibrated, along with both fresh VCM receivers, two reactor transmitters. The installation of the main feeder from the 2500 KVA transformer to the switchgear was completed. The transformer was successfully returned to service. A new deckwriter was installed in the vinyl area control room for laboratory data. The annual transformer service check was completed. There were five mechanical seals repaired this month on pumps and compressors in the vinyl production area and one hot water charge pump was overhauled. Four of the seal failures were in the old module - the seals on the east VCM charge pump, one emission recovery compressor, the chem wash pump, and one recovery compressor had both the inboard and outboard seals replaced. In the new module the outboard seal was replaced on one of the recovery com pressors. All eight of the reactors and condenser safety disc and holders have been changed to the newer style. The VCM charge header plugged with polymer in the old module and was removed for cleaning. The bottom of the fresh VCM receiver also plugged and was opened to remove the polymer buildup. -8- DTH 000019265 MECHANICAL - (continued) A major shutdown in the new reactor module was taken to clean equipment, repair process and steam leaks, and to PM some equipment. The shutdown work was completed without any injuries. There were four major repairs to the vinyl dryers and Bird centrifuges. The dryer repairs were to replace a trunion roller on #7 dryer and to resecure the driving gear on #1 dryer. The Bird centrifuge repairs were to #2 centrifuge and the #5 centrifuge. The #2 centrifuge was removed for cleaning and the gearbox replaced. The gearbox and the antichatter device were replaced on #5 centrifuge. All three manual baggers were repaired. Several level indicators and torque controllers were calibrated. Repairs were also made to the pneumatic transfer activators. Seals were replaced in the north and middle slurry pumps for the large blend tanks. One slurry pump motor was repaired. The agitators were removed and blind flanges installed on the 407 and 501 slurry blend tanks. Ball check valves were installed in the air sparge lines to both large slurry blend tanks. Compound-Dry Blend-Plasticizer and Silo Storage Major repairs to the compound lines were to replace the scrap conveyor belt on Line III and reworking the "B" blender gearbox base on Line III. The Hoffman blower on the vacuum cleaning system was replaced. Other repairs consisted of minor leak repairs and dicer maintenance. A new DC controller was installed for the Line III pull roll. The Line I scales were calibrated and repaired. Repairs in the plasticizer unit were to replace the bearings on both blower units, repacking and seal repairs to the plasticizer pumps on three tanks. The seals were replaced in the new plasticizer filter. R4 reactor was inspected by the MED inspector and a repair was made to the heating coil as a result. Safety discs were replaced on three plasticizer reactors. A new level gauge was installed in the phthalic anhydride feed tank. One of the Welex motors in the dry blend unit failed and is currently being repaired. The blender product blower controls were calibrated. The Orbitran control system spares were completely checked and are now functional. The boots were replaced on the Kason screeners. Utilities and Service There were four repairs to the plant instrument air system. Valves were repaired in two air compressors and one motor repaired. The air and oil wipe packings were replaced in one air compressor. The heater elements were replaced in the #3 air dryer east tower. The pump shaft was replaced in the #15 cooling water pump. The #1 and #2 boilers were shutdown and the safety system checks completed. Mechanical r DTH 0019266 MECHANICAL - (continued) and electrical repairs were completed to the #5 aerator and it was returned to service. Service personnel were in to replace 20 regulators in the propane vaporizers. The control panel on #3 vaporizer was also replaced. The compressor was replaced on Line III chiller and the starter repaired. Miscellaneous The initial training program for the various Orbitran controllers in the plant was started. Additional training sessions are now being planned. Several mechanical training sessions for various topics were also started. -10- DTH 000019267 PERSONNEL - J. L. Carter EMPLOYMENT Don W. White, Mechanical Engineer Alonzo McKnucle, Casual Labor Bobby Trimble, Casual Labor Eugene Mays, Casual Labor Larry Hubbard, Casual Labor Clyde Neely, Casual Labor Maruice Edmond, Casual Labor Gary McFarling, Casual Labor John Smith, Casual Labor TO/FROM LEAVE OF ABSENCE None. TRANSFER/PROMOTION John Hull, General Mechanic "B" to General Mechanic "A" Edward Mize, Electrician "B" to Electrician "A" William Phillips, General Mechanic "B" to General Mechanic "A" Bobby Ward, General Mechanic "B" to General Mechanic "A" George Carnathan, General Mechanic "A" to Electrician "B" RETIREMENT None. TERMINATION Gary McFarling, Casual Labor Maruice Edmond, Casual Labor John Smith, Casual Labor Clyde Neely, Casual Labor Larry Hubbard, Casual Labor Eugene Mays, Casual Labor DEATH/DISABILITY None. OTHER During the month of April there were nine (9) casual labor employees on payroll. Total hours worked were 1551. The bulk of these employees were utilized for bagging resin. -ll- DTH 000019268 CONOCO Cl!l Ml CALS Aberdeen, Mississippi April 1980 MONTHLY PERSONNEL REPORT -alaried Employees iourly Employees 79* 157 Minority Employees " Salaried 7** 0. '0 8.9%** Lotal Employees :.mployees (Hourly) 236* Hourly Total 62 69** 39% 29%** New Employees ' Terminations _____ 0 0 Hourly Min. Hired % Min. Hired Hourly Min. Term. % Min. Term. ____ 0 0 ____ 0 DEPARTMENTS PAR # EMPLOYEES MIN. EMP. % MIN. NEW HIRES YTD TERM. YTD TURNOVER YTD Warehouse 9 9 2 22% 0 0 0 _o_ JL_ _Q___ Sen. Plant Maintenance 11 46 11 46 6 54% 7 15% 0 2 01 JO__ 1135. 0 0 00 0 0 Laboratory Compound 22 41 20 35 3 15% 28 80% 0 0 00 0 0 0 0 2*** 0 0 2.8% 'inyl 'lasticizer 32 5 32 4 13 41% 3 75% 0 0 00 0 0 0 00 0 0 0 Cumber of Applicants: Hires (Hourly) Month 13 Year to Date 47 Month 0 Year to Date 2 VPPLICANT BREAKDOWN: f Minority 7 o Minority !f Female 1 % Female 54% 7.7% Includes two (2) temporary employees. Terminations (Hourly) : Month 0 Year to Date 3*** Overall Turnover 0 Projected Annual Turnover 13% Includes one (1) temporary employee. Includes one (1) retirement and is not counted in turnover rate. -12- DTH 000019269 (2) Non-Control Table Overtime - th a t overtim e due to working re g u la r hours on a holiday and working re g u la r hours on the s ix th day in operations. a> 4- (O Q 03 E 4o-> 1-- ins 4-3 (L3 x >Ol f0 S- r-- 4~> to LO -4-> o M- 1-- O S_ <o 0) x to 4-3 <o o 03 o c to 03 to to 03 X) c c o o o <0 CM a> OCL So .a < COo cCOt CTi o < i- CL < E .P T 5 s- iO) 4-> > CO o o o 6A (fc \ CO Vi LO \ ^ ! r*- CO \| CM \ 1 i i 1 r" \ CTi i r__ csj '0' ooo o o ooo o o O to 0^*0CO- O VO r-- CO CM Vr-O 45--> 03 > o o LO r-* o o VO CM 03 E -a hr-- ^a s- r4-j 3o cn *r- i/i to i- so CO cr CM o o s *3" CT CO Oo oo CO0O0 03 E 03 E 0) 4-3 F-- c 4-3 cu u s- 10 03 O C 0> 0) to c to L? O -o P S- 3 O x c 40-33 4-> Lo. c 3 o KJ CO o_ <o 4-3 U > f-- O 4J 4-* t1o_ h- to a. 03 i- CO -O o. E >> c 40 to ri---- 03 c a ns 03 to o 4-> 03 Q 3 s _J o > Cl. ZD CD DTH 000019270 PROCESS ENGINEERING - R. A. Frohrelch A. Specialty Compound Line Efforts to eliminate the hard particle problem in the finished compound have been unsuccessful. Tests using larger diameter screw elements were conducted, but did not reduce the number of hard particles. A test run using a compounder with a longer screw is scheduled for May at WernerPfleiderer's New Jersey laboratories. Further testing will be conducted in June at Werner-Pfleiderer's German location to evaluate mechanical changes required to eliminate the hard particles. B. Centrate Rinse Mater Design The class "A" process design for this project is being prepared. C. Breathing Air Modifications The class "A" process design is being revised to provide for an in-house design of an air-water separator for the existing Nash Compressors. D. Compound Line III Debottlenecking A review meeting for the design was held in April. A test utilizing a borrowed set of No. 7 rotors in the Farrel Continuous Mixer will be conducted to determine if production rates and quality can be improved by the proposed changes to the compounder. E. Compound Die Face Pelletizer The class "A" process design was issued and a review meeting for the project was held. F. Reactor Agitator Replacement During the review meeting for this project it was decided to provide the new model Lightnin gearboxes for this project and to return to a seal oil system rather than to continue to use a seal water system. G. Old Module Hot Water Tank Replacement A class "A" process design for this project was issued, the definitive estimate was completed, and an AFE request was submitted. H. V-ll Water Stripper Tank Replacement A class "A" process design to replace the existing V-ll water stripper tank with a surplus tank is being prepared. The existing tank needs to be replaced for safety and environmental reasons. I. Resin Reclaim System * Resin slurry from one of the concrete settling pits has been dried and bagged. The dried resin will be sent to potential customers for their evaluation. The class "A" process design for the project is being prepared. -14" DTH 000019271 J. Biodisc Study A process design for the installation of a pilot rotary biological disc unit to treat effluent from the API separator is being prepared. Since approximately 70% of the BOD loading to the waste treatment ponds comes from the API separator, a reduction of BOD for this stream will greatly reduce the pond loadings. K. Dissolved Air Flotation Tests Results of the dissolved air flotation tests on the API effluent were issued. The tests show only a 20% reduction in COD levels of the effluent is obtainable with this technique. No further testing is planned. M. Initiator Injection Pot Replacement A class "A" process design to replace the existing initiator pots with pots of a higher design pressure and larger relieving area is being prepared. N. Dual Steam Stripping Instrumentation A class "A" process design to automatically switch steam flow from the open four inch nozzle to the nozzle with the sparger during the latter portion of the recovery operation is being prepared. Reactor vibration is significantly reduced with the steam injected through this sparger. O. Kemp Air Dryer Evaluation A Kemp service representative was in the plant to thoroughly evaluate the existing air dryers. Recommendations include inlet filter to remove entrained water ahead of the dryers and possible piping modifications to balance air flow to the dryers. P. Groundwater Monitoring Two consulting firms were contacted concerning groundwater monitoring around the resin settling pond. Both firms will visit the plant and prepare proposals to determine if organics are leaching from the pond. Q. Rupture Disc Survey A survey of all rupture discs used in VCM service is being prepared. R. Firewater Improvements - Phase III The class "A" process design for the project is being prepared. S. Resin Exapansion Project Plant review and approval to purchase various equipment items is con tinuing. Piping drawings and equipment layout drawings are being reviewed and approved. PED issued the class "A" process design for the fluid bed dryer incorporating all recent changes to the design. -15- DTH 000019272 ENVIRONMENTAL - V. E. Messick I. Particulates The compliance report for particulate testing performed in March was submitted to the Mississippi Bureau of Pollution Control. Particulate testing was preformed on one dryer. II. Water BOD and COD levels were within NPDES permit limits. A 24 hour static bioassay was conducted by Applied Biology of Atlanta on pond number 6 effluent. Results were 100% survival in 100% effluent. The quarterly NPDES report was prepared and submitted to the Mississippi Bureau of Pollution Control. -16- 000019273 DTH Flow GPM Jan. - Ave. 810 Max. 941 Feb. - Ave. 645 Max. 802 Mar. - Ave. 595 Max. 743 Apr. - Ave. 628 Max. 877 May - Ave.' Max. June - Ave. Max. July - Ave. Max. Aug. - Ave. Max. Sept. - Ave. Max. Oct. - Ave. Max. Nov. - Ave. Max. Dec. - Ave. Max, TABLE I - WATER COMPLIANCE WITH NPDES PERMIT PARAMETERS BOD PPM LB./DY. 43 436 131 1342 6 42 8 56 29 220 36 314 COD PPM LB./DY. 86 851 216 2214 15 116 24 171 66 502 95 828 Sus. Solids PPM LB./DY, 11 103 13 143 10 79 13 125 11 74 14 94 21 147 30 232 54 378 67 519 12 86 13 129 Diss. 02 6.8-8.5 6.7-7.9 6.6-8.3 6.4-8.3 NPDES - Ave. _ Max. _ 32 387 43 520 - 1390 - 1940 - 605 - 909 >6.0 ph 7.7-8.0 7.1-7.8 7.1-7.8 7.5-8.4 6.0-8.5 -17- DTH 000019274 ENERGY CONSERVATION - V. L. Thornhill I. Plant Operations Total energy consumption for April was 92.2 MMM BTUs. The energy consumption per pound of product decreased from 3332 BTU/Lb. to 3282 BTU/lb. in April. II. Plant Energy Conservation Program A. Steam Leaks Forty-one steam leaks were repaired in April. B. Energy Reporting The first quarter energy report was issued in April. The plant had a 24.7% energy savings compared to the 1972 base year. After adjusting for EPA and OSHA projects, the plant energy savings were 38.1% compared to the 1972 base year. -18- DTH 000019275 ITEM 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 1979 APRIL 25.0 3.1 4.9 1.2 34.2 60481 1020 61.691 5.0208 10000 50.208 0 92000 0 111.899 3272 Avg. Stack Temp. 1979 1980 416 387 428 414 463 419 Avg. % Excess Air 1979 1980 100 94 120 24 25 27 1980 APRIL 20.8 1.8 4.2 1.3 28.1 45822 1020 46.738 4.5484 10000 45.484 0 92000 0 92.222 3282 -19- DTH 000019276 MECHANICAL ENGINEERING - J. A. Dixon AFE's Submitted, Approved, and Closed The following AFE's were submitted and approved during April: AFE No. Title Authorized 9600 Calcium Stearate Addition System $ 84,000 9610 API Clean Water Bypass 23,000 9620 Cooling Tower Motor Replacement 17,800 The following AFE was closed to field charges during April: AFE No. Ti tl e Authorized 9049 Repairs to Dryer Inlet Ducts $ 25,000 Completion reports were issued for the following AFE's during AFE No. Title Authorized 9247 Farrel Mixer Feeders $ 47,000 9539 Laboratory Equipment 31.000 9029 Repair of Steam Tracing and Insulation 62.000 9069 Centrifuge Rotors Repair 47,000 9079 Cooling Tower Motor Repair 17,800 Design Design work is in progress on the following projects: Replace T-100 P. A. Tank Automatic Plasticizer-Stabilizers Weigh-up System Revisions to Emission Recovery System Replace Water Stripping Tank Diking of Sphere and Curbing of Drum Storage Areas Replacement of Hot Water Charge Tank Double Block Valves for VCM Charge Methocel Charge Revisions -29- DTH 000019277 MECHANICAL ENGINEERING - (continued) Contracts were let for the following projects: Piping, Concrete and Equipment - Fire Protection Improvements - Phase I Repair of Three Lagoon Aerators Repair of Plant Effluent Outfall Box Installation of Methocel Studding Outlets. AFE Activity 1. AFE 9297 - Automatic Plasticizer Meigh-Up System -- R. B. Harned Engineering drawings are approximately one third complete. 2. AFE 9158 - Fire Protection Improvements - Phase I - J. P. McKee The contract was let for the installation of the piping and equipment. Construction is in progress. 3. AFE 9228 - Dry Blend Silo Alarms - J. L. White Bids were received and evaluated for the installation of the remaining silo alarms. The contract will be let in May. 4. AFE 9609 - Reactor Inert Vent System - J. P. McKee The piping tie-ins were completed in the new reactor area. 5. AFE 9619 - Waste Water Revisions - Part I - J. L. White The sampling weirs and catch basins were installed. 6. AFE 9649 - Double Block Valves for VCM Charge - M. S. Richards The installation of the block valves in the new module is complete. Bids are being evaluated for installation in the old module. 7. AFE 9689 - Diking of Sphere & Curbing of Drum Storage Area - J. L. White Engineering is complete and the basis of bids for installation have been sent out to qualified contractors. 8. AFE 9709 - Facilities for Multiple Grade Resin Production - CED The pumps, dust collector, blower and silo are on order. P & I drawings were reviewed and sent back to CED with comments. 9. AFE 9729 - Fire Protection Improvements - Phase I - CED Quotes have been received for the fire pumps and jockey pump. are being evaluated. The quotes -21- DTH 000019278 MECHANCAL ENGINEERING - (continued) 10. AFE 9759 - Aberdeen PVC Resin Expansion - V. L. Thornhill Plant review of equipment selection and layouts is continuing. The resin storage silos, slurry blend tanks, and initiator storage system were released for purchase. The area electrical classification drawings are being prepared by Li twin. General arrangement drawings of the product screeners, weigh belts, and product rotary valves and electrical substations were reviewed. 11. AFE 9769 - Automatic Setback Thermostats - R. B. Harned Installation of thermostats in all offices is complete. 12. AFE 9570 - Replace T-100 P. A, Tank - J. P. Windham Engineering is substantially complete. A design review will be scheduled. Material purchases are in progress. CONSTRUCTION - G. A. Morgan The installation of double block valves for VCM charge in the new module was completed. Automatic setbact thermostats were installed in all office areas. Defects in the new reactor condenser flanges were repaired and machined to the desired flatness. Recovered VCM, 401 and 701 receivers were cleaned during the period. Repairs were completed for the leaking PIV valve and 14 inch plant water line. Structural repair's were completed for one of the lagoon aerators. There were six contracts and 57 register tickets issued for contractor work during the period. -22- DTH 000019279 (1) Thru March, 1980 Actual Accounting (2) Thru April, 1980 \UIII. CAPITAL NO. oiisi'K i ition ABliKIMliN Airi'HOU I NATIONS RII'OItT DATIi Airm. AITROVHD AIT AMT. (11 o l: INAL LXITNITl) COMMUTED TOTAL UST. TO OATH TO DA IT. COST COMP. UNPI.lt (OVER) AUTII. AMT. liST, ilST. in i'5 <_>s. REMARKS 9237 Heated Plasticizer Addition System 9297 Automatic Plasticizer-Stabilizer Weigh-Up System 9098 New Compound Line 9148 Plasticizer Chemical Exposure Abatement 9158 Fire Protection Improvements Phase I 9188 Railcar Resin Heel Clean-Up System 9228 Dry Blend Silo Alarms 9248 Silo Isolation Valves 10/11/77 12/14/77 37,000 60,000 13,090 56,293 13,518 57,944 37,000 60,000 4/17/78 2 ,050,000 2,089,061 2 ,101,962 2,101,962 8/21/78 152,000 141,706 146,633 152,000 9/19/78 176,000 105,028 164,521 176,000 10/12/78 12/13/78 12/14/78 55,000 25,000 25,000 42,970 4,392 21,327 42,970 9,368 22,244 55,000 25,000 25,000 9258 Dryer Operation Improvements 9519 Critical Spare Equipment 9549 Safety Equipment 9559 Color Weigh Room Modifications 9589 Instrument Air Dryer 12/14/78 2/6/79 3/26/79 4/19/79 5/30/79 315,000 175,000 15,000 25,000 110,000 260,397 272,438 97,432 159,168 12,326 14,933 16,921 16,962 90,275 91,318 315,000 175,000 14,933 25,000 110,000 9609 9619 9269 Reactor Inert Vent System Waste Water Revisions - Part I Air Compressor 6/28/79 7/3/79 7/9/79 90,000 140,000 340,000 5,326 8,460 128,109 134,589 208,024 239,930 90,000 140,000 340,000 0 6/80 9/80 0 6/80 9/80 Design in progress. Design in progress. (51,962) 12/79 4/80 0 6/80 9/80 Closed to field charges. Revisions in progress. 0 6/80 9/80 Installation in progress. 0 6/80 9/80 Project operational. 0 5/80 8/80 Bids being evaluated. 0 5/80 8/80 Eighteen of twenty-one valves installed. 0 9/80 12/80 Project operational. 0 6/80 9/80 Purchases proceeding. 67 10/79 6/80 Closed to field charges. 0 7/80 10/80 Project operational. 0 6/80 9/80 Winterization design in progress. 0 6/80 9/80 Engineering in progress. 0 5/80 8/80 Project operational. 0 6/80 9/80 Project operational. 9639 9649 9659 9669 9679 9689 9699 9709 9719 9729 9739 9749 9759 9769 9510 9520 9530 9540 9550 9560 9570 Revisions to Emission Recovery System Double Block Valves for VCM Charge P. A. System Modifications New Air Header Plant Winterization Diking of Sphere & Curbing of Drum Storage Areas Plant Dryer Debottlenecking Facilities for Multiple Grade Resin Production Aberdeen PVC Resin Expansion (Partial) Fire Protection Improvements Phase II Kethocel Charge Revision Improved Rupture Disc Holders Aberdeen PVC Resin Expansion Automatic Setback Thermostats Miscellaneous Projects Under $10,000 Replacement Phthalic Anhydride Tank Spare Incinerator Laboratory Equipment P, A. Handling Improvement Safety Equipment Replace T-100 P. A. Tank 7/12/79 100,000 7/18/79 7/10/79 8/15/79 9/5/79 9/15/79 182,000 35,000 25,000 64,000 170,000 9/15/79 9/20/79 80,000 870,000 9/10/79 850,000 10/1/79 490,000 10/3/79 66,000 10/22/79 27,000 12/10/79 11 ,150,000 12/31/79 3,000 1/3/80 150,000 1/17/80 75,000 1/23/80 2/6/80 3/3/80 3/12/80 3/27/80 650,000 45,000 63,000 25,000 119,000 17,310 53,513 100,000 67,626 25,499 15,727 55,651 0 93,824 182,000 32,451 35,non 16,106 25,000 61,536 61,944 802 170,000 0 0 80,000 0 0 870,000 11,421 772,000 850,000 0 0 490,000 0 14,396 66,000 24,495 24,495 24,495 236,485 2 ,086,850 11,150,000 128 2,124 3,000 36,977 81,247 150,000 69,654 80,875 84,000 0 0 16,685 0 0 0 41,604 20,081 1,630 5,708 650,000 45,000 63,000 25,000 119,000 0 6/80 9/80 Installation in progress. 0 6/80 9/80 Installation in progress. 0 6/80 9/80 Project operational. 0 6/80 9/80 Project operational. 2,056 3/80 6/80 Closed to field charges. 0 6/80 9/80 Bids requested. 0 9/80 12/80 Engineering in progress CED. 0 9/80 12/80 Engineering in progress CED. 0 9/80 12/80 Equipment on order. 0 10/80 1/81 Engineering in progress CED. 0 8/80 11/80 Engineering in progress. 2,505 4/80 7/80 Closed to field charges. 0 7/81 10/81 Engineering In progress. 0 6/80 9/80 Project operational. 0 12/80 3/81 Forty projects approved. (9,000) 6/eo 9/80 Project operational. 0 1/81 4/81 Engineering in prooress CED. 0 8/80 11/80 Purchases proceeding. 0 12/80 3/80 Engineering in progress. 0 9/80 12/80 Purchases proceeding. 0 9/80 12/80 Enqinocrlnq in progress. DTH 000019280 Ainu. CAPITAL NO. description 9580 9590 9600 Boiler Economizers Critical Spare Equipment Calcium Stearate Addition System 9610 API Clean Water Bypass ABiimnIliN AUTHOR 1'CATIONS REPORT (1) Thru March, 1980 Actual Accountlnq (2) Thru April, 1980 DATE Aimi. APPROVED AH: AMT. (U C) PINAL UNDER EST. EST. EXPENDED OftMITTKD TOTAL EST. (OVER) COMP. CLOS. TO DATE TO DATE COST COMP. AtJTH. AMT. DATE DAT!: REMARKS 3/26/80 140,000 0 0 140,000 0 10/80 1/81 Engineering In progress. 3/26/80 59,000 0 0 59,000 0 10/80 1/81 Update quotes requested. 4/2/80 4/15/80 84,000 23,000 0 0 84,000 0 0 23,000 0 11/80 2/81 Engineering In progress. 0 8/80 n/8o Engineering In progress. EXPENSE 9049 Repairs to Dryer Inlet Ducts 9089 Vibration Study-Capacity Replacement Reactors 9/13/79 10/29/79 25,000 50,000 19,038 27,299 19,038 27,433 19,038 30,000 5,962 4/80 7/80 20,000 6/80 9/80 Closed to field charges. Project complete. -24i DTH 000019281 LABORATORY - R. D. Jackson CUSTOMER COMPLAINTS Customer Product Complaint Reported By Polysar Inc. World of Plastics World of Plastics 5305 5385 5385 Low bag weights Foreign contamination - rocks Foreign contamination - rocks CRM CRM CRM WAIVERS RECEIVED Date 4/1 4/2 4/2 4/7 4/7 4/7 4/10 4/18 4/18 4/18 4/18 4/23 4/25 4/29 TOTAL Identification T-2481 PLCX-42673 C0NX-45280 PLCX-43738 CONX-42962 C0NX-45707 PTLX-41605 01902 Bags 01959 Bags T-2481 PTLX-41862 T-2870 CONX-45263 PLCX-43230 14 Product Customer Reason Waived By 5385 5465 5385 5385 5305 5305 5425 5385 5385 5305 5385 5305 5465 5385 World of Plastics Industrial Plastics Mastic World of Plastics N. J. Terminal N. J. Terminal Uni royal Export Export Celanese Pipe Charlotte Pipe Intex 3M World of Plastics Particle Size Bulk Density Particle Size "B" Color Value "B" Color Value "B" Color Value Gels Particle Size Particle Size Viscosity Particle Size Viscosity Bulk Density Particle Size RDJ CRM ELK ELK RNG RNG CLS ELK ELK ELK ELK RDJ JRW ELK PRODUCT DEVELOPMENT AND SERVICE Date 4/1 4/1 4/1 4/1 4/4 4/4 4/4 4/8 4/9 4/9 4/9 4/10 4/11 4/11 4/14 4/14 4/15 4/15 4/17 4/17 Product Quantity Qbs.) Customer 5385-1 2 5305 2 17461 Blk. 50 15041 Cl. Bl. 50 50 34551 Nat. 10 34641 Blk. 10 35851 Gry. 545 10 17461 Nat. 100 27121 Blk. 50 26421 Nat. 50 16851 Cl. Bl. 50 50 5305 50 38601 Nat. 10 15641 Cl. Bl. 50 100 38601 Nat. 100 5385-1 4 x 20 39261 Clear 50 16851 Cl. Bl. 50 50 5385-1 10 5425 10 Oatey Company Oatey Company Homestead Plastics Homestead Plastics Conoco Inc. Conoco Inc. Conoco Inc. Plastic Profiles Inc. Troxel Mfg. Co. Troxel Mfg. Co. Homestead Plastics Uniroyal Chemical Division ITT Royal Electric Anchor Wire ITT Royal Electric RJR Filmco Circle F/Sylvania Conoco Inc. Bata Shoe Bata Shoe -25- Requested By JTW JTW JFN JFN JAP JAP JAP - JFN JFN JFN NTH NTH JFN NTH ELK RNG ELS RNG RNG DTH 000019282 LABORATORY - (continued) Date Product Quantity (Lbs.) Customer Requested By 4/18 4/18 4/22 4/22 4/22 4/22 4/22 4/22 4/22 4/22 4/23 4/23 4/23 4/23 4/23 4/25 4/25 4/25 4/25 4/25 4/25 4/25 4/25 4/25 4/30 4/30 VRP 16851 Clear 35851 Nat. 34641 Blk. 35441 Nat. Sifter Overflow 5385-1 5425 J-40 Methocel J-40 Solution 26421 Nat. 27121 Blk. 27121 Blk. 27121 Nat. 28831 Blk. 5305 5385-1 5425 5465 80172 B 80273 G 90171 35851 Nat. 5465 35851 Nat. 28831 Blk. 1 Quart 50 6.6 6.6 6.6 10 1 10 4 x 50 5 gal. 50 50 50 50 50 50 50 50 50 5 5 5 50 50 50 5 Heritage International Lavanture Products Techni Chemical Products Techni Chemical Products Techni Chemical Products Heritage International Fritz Airfreight Zapata Industries Conoco Chemicals Conoco Chemicals Hadley Molded Products Hadley Molded Products Fritz Airfreight Fritz Airfreight Fritz Airfreight Whitaker Chemicals & Coatings Whitaker Chemicals & Coatings Whitaker Chemicals & Coatings Whitaker Chemicals & Coatings Whitaker Chemicals & Coatinqs Whitaker Chemicals & Coatings Whitaker Chemicals & Coatings Interstate Wire Bel den Corp. Interstate Wire Conoco Inc. DS AHH WRP WRP WRP DSS JPM WBS PAS PAS AHH AHH JPM JPM JPM AHH AHH AHH AHH AHH AHH AHH - MAS - JAP Special Compound Testing Six (6) lots of compound were tested and compared with Western Electric specifications. There were four (4) lots of 36861 Natural and two (2) lots of 34861 Gray 546. One lot of 36861 Natural was high in plasticizer content; the other lots met specifications. One lot of 34533 Natural for Packard Electric was tested and found acceptable. One lot of 34431 Natural was tested and found to meet Phelps Dodge specifica tions. QUALITY CONTROL TESTING Resin Regular Samples = 234 Bag Blends = 139 Other In-Process Samples = 1746 Bulk Shipments = 119 (Railcars = 75; Trucks = 44) -26- DTH 000019283 LABORATORY - (continued) Dry Blend Blenders Produced = 250 Blenders Tested = 215 Blenders Adjusted = 12.0% Other In-Process Samples = 163 Bulk Shipments = 15 (Railcars = 4; Trucks = 11) Compound Blenders Produced = 681 Blenders Adjusted = .9% Other In-Process Samples = 73 Bulk Shipments = 21 (Railcars = 13; Trucks = 8) Resin Heat Stability Oven heat stability tests were run on forty-four (44) blends of resin. 5385 5425 5305 5465 16 Blends 16 Blends 8 Blends 4 Blends Only one blend (5385) was significantly poor than the control. Raw Material Testing Sixty-eight (68) lots of plant raw materials were tested. A small amount of a lot of SP-33 clay that was rejected in March reappeared in 2 truck loads received in April. It was rejected and a complaint was filed with the supplier. Approval has also been withheld on one lot of gray color concentrate until acceptable color tolerances are established. RVCM of Shipment Samples A total of 159 samples of resin were tested prior to shipment for RVCM. Eleven of these were rejected for residual content. Following is a summary of the shipment RVCM testing results: Product 5305 5385 5425 5465 Average ppm RVCM 3.0 2.0 0.9 0.2 No. samples 79 33 31 5 -27- DTH 000019284 LABORATORY - (continued) SPECIAL PROJECTS RVCM of Slurry A total of 456 samples of slurry were tested for RVCM in April. The over all average was 258 ppm. There were two days during the month the slurry RVCM average was above 400 ppm. RVCM of Blowdown Tanks A total of 132 samples of water from the blowdown tanks were tested for RVCM. The overall average for April was 3.6 ppm. RVCM of 5305 Resin from Drier A total of 45 samples of 5305 resin from the driers were tested for RVCM. The overall average was 9.2 ppm. Resin Volume Resistivity Volume resistivity tests were run on 5425 and 5465 resin samples. The six samples gave uniform, high values for VR. Metrastat Oven The new Metrastat heat stability oven has been modified to give good temperature uniformity from the door to the back of the oven. A large number of resin samples have been exposed both in the Metrastat and the Blue M conventional forced draft oven. There was good agreement of results for most samples; however, occasionally the two ovens gave results which were not exactly the same. Plans for the future include tests to determine day-to-day reproducibility of Metrastat results, a recheck of center to wall temperature uniformity in the oven, and tests to see if exposure tests on the raw resin correlate with results on a compound containing the resins. Line V Start-Up Laboratory Wei ex blending tests were run to compare the current Line V procedure with one suggested by Werner & Pfleiderer. The Werner & Pfleiderer procedure gave little or no reduction in hard particles. EQUIPMENT Schott Automatic Viscometer This new unit was received and installed. Start-up of the viscometer was very smooth and trouble free, ft has permitted us to analyze up to 30 samples a day, including all bulk shipments, compared to a maximum of -28- DTH 000019285 LABORATORY - (continued) six samples in the same man-hours by the manual method. F-42 Perkin Elmer Equipment problems on the F-42 which had caused the need for manual injection of samples during several days of the month have been corrected. -29- DTH 000019286 TRANSPORTATION - J. E. Stark Shipment by Product - M/lbs. Resin Plasticizer Dry Blend Compound Total APRIL 132Q5 156 813 3418 17592 Year-tO'Date 75264 199 . 7553 14161 97177 Number of Shipment by Mode R/C O.T. C.C. C.O.T TOFC' CPU TOTAL Resin - Bulk Package Export - ABR Plasticizer - Bulk Dry Blend - Bulk Package Compound - Bulk Package 60 9 Export - Package Back Hauls for April 69 33 3 42 2 7 8 28 .4 127 20 1 4 5~ 1 6 1 9 4 9 2 5 ~W 93 13 42 4 11 9 17 37 4 230 Number of Shipment by Month-Year-To Date January February March April R/C 104 111 130 ' 69 O.T. Bulk 53 83 95 43 O.T. Van 72 66 64 84 c.o:t. 0 0 1 0 TOFC 2 4 0 0 CPU TOTAL 36 273 35 320 48 375 29 230 -30- DTH 000019287 LOCATION MAIN-East ' TOTAL M SQ. FT. 48 Prairie 12-1 12-2 12-3 12 22 21 12-4 12-5 22 21 12-6 21 12-7 12-8 12-9 21 21 21 Total 209 CONTENTS Compounds Dry Blend Export Resin Conoco Resin Compound Resin Export Resin Conoco Export Resin -- 3 4___ .. .-1 1___ .4 1.2 3. 5 ESTIMATED MM POUNDS , ON FLOOR OPEN TOTAL t;.R & .5 ' 10.0 1.2 * .3 1.5 3.5 . 3.5 3.5- . 3.5 Conoco Resin 4. 5 Resin O.G. - Mill Scraps -- -1 Cmpd 0. 6. -- 1- 0___ Dry Blend 0. G. .1 Sifter Overflow .2 Resin 0. G. .7 4-5 . 3.5 2.1 .4 2.5 Compound Dry Blend Raw Material Resin 0. G. Conoco Conoco Resin Sub-Total (Plug-Aisles) __________ 2. 9 .2 4. 0 4. 5 1. 8 3.2 4.0 4.5 1.8 .3 . . 1.7 3.5 3.5 3.5 3.5 38.5 2.5 Total Conoco ... 33,8 7.2 41.0 DTH 000019288 \ SAFETY REPORT Lost Time Accident Doctor Cases First-Aid Cases Man Hours Worked APRIL 0 0 2,390 Y.T.D. GRAND TOTAL SINCE L.T.A. 9,563 151,238 MATERIAL HANDLING REPORT M/Lbs. 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 6115 2835 4334 0 364 162. 4091 1863 1417 '21,181 LABOR REPORT Total regular Hours Total Overtime Hour Total Worked Paid but not Worked Total 170? 208 1910 _____ 80 1990 Labor Efficiency equals 21.2 MM/Lbs. - Hours Worked Overtime % 10^ 11>090 . T/L 151 70 107 0 9 4 101 ' 46 35 523 -32- DTH 000019289 EQUIPMENT REPORT Lift Truck Hours Worked Gal of Fuel Consumed Gals/Hrs 378 596 1.6 Lift Truck Efficiency Equals 21.2 MM/Lbs. - Hours Worked *-56032 Lbs./hr OFF-GRADE IN STORAGE MATERIAL M/Lbs. Sifter Overflow Resin "BC" 98,595 ' 4,916,601 Resin "H" Mills Scraps Compound "B" Compound "H" Dry Blend "O.G." Total 1,741,352 76,417 713,445 . 150,100. 86,115 7,782,625 T/L 2 121 43 2 18 4 2 .192- D.F. OPERATION Total inventory of packaged product increased approx 4MM lbs. during the month. Most of the increase was due to resin production. Export shipments picked up some from the previous month. Due to the resin build-up we had to lease a warehouse at Prairie outside our complex. Safety Safety meeting held during the month on housekeeping, especially oil spills on floor and. loose objects laying around that could be a trip hazard. -33- DTH 000019290 ABERDEEN RAIL CAR REPORT % SURFACE TRANSPORTATION DEPT. AS OF 4/30/80 LIMITS LOCATION LOADED VCM 35 IN PLANT 25 MONROE LEAD 10 39 20 BINFORD ICG DOWNTOWN TEXICO TRACK SLSF ACROSS BRIDGE STRONG 30 PRAIRIE 50 EGYPT , , OTHER 160 TOTALS 49 EMPTY HOPPERS 8 16 LOADED HOPPERS 16 2 11 4 24 1 "31 61 OTHER LOADS 1 3 TOTAL 35 60 11 1. 31 4 138 RECAP FOR MONTH 4/2/80 4/8/80 4/16/80 4/23/80 35 30 36 28 27 29 33 25 5Q 56 68 64 5 120 4 124 4 128 3 125 PAT WELLS -34- DTH 000019291 rc T INJURY FREQUENCY* X 100 DTH 000019292 ABERDEEN OSHA RECORDABLE INJURIES ABERDEEN FIRST-AID CASES MONTHLY HOURLY TURNOVER DTH 000019293 ENERGY USAGE ( C i. c e Month DTH 00001g294 12 Month Moving Average BTU /LB. ABERDEEN PLANT PRODUCTION <CQO 5 DTH 000019295 08 61 ooo ft* O CO o o N) Lti > OO OO O o ofc. o 1M ABERDEEN PLANT INVENTORIES