Document yk864OkprY0on3oe1G6oRNEoV
To: R. T. Ferrell
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Interoffice Communication
From: Date:
Subject:
J* W Were April 16, 1987
ABERDEEN MONTHLY PROGRESS REPORT MARCH, 1987
There were two first aid cases and three medical treatment cases recorded during the month of March. One of the medical treatment cases required restricted work activities. As of March 31, 1987, the plant had operated 2,824 days or 3,629,206 manhours without a lost time injury.
PVC resin production for March was 34.1MM pounds. Mechanical downtime in the reactor areas was due primarily to agitator seal repairs on 400 and 743, safety disc replacement on 743, spray nozzle revisions to 741 and 742, agitator gearbox repairs on 742 and 745, new module Modicon replacement and recovery compressor repairs. Resin production year-to-date totaled 211.9MM pounds. The VCM efficiency for March was 1.01525 pounds of VCM per pound of PVC produced versus a 1.00208 standard. Year-to-date VCM efficiency is 1.01139.
Compound production for March was 7.3MM pounds. Line I and Line III operated thirty-one days and Line V operated 14.5 days during the month. Production was limited primarily by product changes and maintenance on Line V. Year-to-date compound production was 42.7MM pounds. Quality performance for flexible compounds was 1.3% off-grade of which 94% was due to mill scrap. "BC,f production was 0.9%.
Dry blend production was 4.6MM pounds for March and 27.1MM pounds fiscal year-to-date. Production was limited primarily by product changes and quality control problems. Quality performance for the month was 97.6% customer grade.
The plasticizer unit operated thirty-one days in March to produce 2.0MM pounds. Year-to-date plasticizer production is 11.4MM pounds.
A one-day training course on problem solving techniques and involvement teams was conducted during March for Vinyl and Laboratory personnel. The first maintenance involvement team conducted a management presentation and a new team was formed in the warehouse.
Total energy consumption for March was 116.861 MMM BTUs. The energy consumption per pound of product was 2434 BTUs, resulting in an adjusted CMA reduction of 52.3%. The adjusted CMA reduction for fiscal 1987 year-to-date is 53.9%.
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R. T. Ferrell 04/16/87 Aberdeen Monthly Progress Report
The total plant variable cost variance for March was $489.9M unfavorable, resulting from an overall unfavorable price variance of $369.4M and a net unfavorable efficiency variance of $120.5M. The total fixed cost variance for March was $59.5M favorable.
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DISTRIBUTION HOUSTON
PONCA CITY
OKLAHOMA CITY LAKE CHARLES VCM PLANT LAKE CHARLES CHEMICAL PLANT BALTIMORE HAMMOND ABERDEEN
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- J. D. BURNS
- R. E. LEHMKUHL
- R. T. FERRELL
- R. D. GAMBLIN
- J. J. LANGFORD
- R. E. SWANTKOWSKI
- D. F. HARMAN
- H. R. FLAMMER
- R. R. SMITH
- S. K. SABORSKY
- K. J. EGGERS
- D. H. SANDERS
- S. E. MCGUIRE
- R. L. POE
- H. J. HALL
- C. M. STARKS
HARRY GARRISON
-DICK CONRAD
- J. A. DEBERNARDI (COVER LETTER ONLY)
- T. H. HUFFMAN
(COVER LETTER AND SAFETY PORTION)
- R. W. SEYMOUR
(COVER LETTER AND SAFETY PORTION)
- J. B. MAHER
(SAFETY PORTION ONLY)
JF, JWW, DWH, PJK, TFL, RAF, KLF, RAM, VEM, HGC, CWT, REP, VLT, JEL, JGC, RBN
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SAFETY - J. V. UPTAIN
Occupational Injuries
March
Fiscal Y.T.D, 1987
Fiscal Y.T.D 1986
First Aid OSHA Recordable
Total Injuries Number of Restricted Workday Cases
(RWC Rate) Number of Lost Workday Cases
(LWC Rate)
2 3 5 1 (4.9) 0 (0.0)
6 4 10 1 (0.8) 0 (0.0)
11 3
14 2
(1.7) 0
(0.0)
Injuries by Department
Vinyl Operations Compound Operations Maintenance Laboratory Receiving/Warehouse Office
Totals
12 11 15 00 22 00 5 10
3
3
*
5 0
0
3
14
Injuries by Type
Cuts and Abrasions Eye Injuries Burns Bruises Strains/Sprains Stings Other
Totals
15 11 00 00 34 00 00 5 10
4 2 4 1 1 0 3 15
Non-Occupational Injuries
v
Lost Workday Cases Days Lost
02 0 11
3 35
Safety Record
Last lost time injury
7/5/79
Days since -
2,824
Manhours since -
3,629,206
OSHA Recordable Injuries
Three OSHA recordable Injuries occurred during the month. One of them, a restricted workday injury, was a back sprain suffered by a compound employee while charging bags of resin into the dry blend master batch system.
The two medical treatment injuries involved: a lacerated finger, pinched between metal shelving and the shaft of a motor being moved by a warehouse supervisor, and a foreign object lodged in the eye of a mechanic who was opening the bottom manway of a vinyl reactor.
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SAFETY - Continued
Training
Topics for the plant safety meetings during the month included: Chlorine Handling Safety, Off-the-Job Safety, Chemical Health Hazards, Boating Safety, Driving Safety, and Maintenance Weekly Safety and Job Review.
Health
Activity for the month included routine dosimetry (shown below) and the completion of annual, medical health screening (van).
Chemical
L. Number
PEL Percent
_> Number
PEL Percent
*
VCM Lead Total Particulates
74 22
2
97.4 100.0 100.0
2 2.6 0 0.0 0 0.0
One of the VCM overexposures occurred without respiratory protection.
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QUALITY IMPROVEMENT PROCESS - R. B. Newton
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The Vinyl Department and Laboratory attended a one-day training course on problem solving techniques and involvement teams.
Drawings of the revisions to the 600 series silo hook-up station (as recommended by the vinyl cross-contamination team) were issued for review.
An involvement team was formed to improve the handling of customer returns at the plant. This came as a result of studies by warehouse personnel showing that substantial savings are possible from improved handling of customer returned material.
The maintenance involvement team that prepared the preventative maintenance program for the new plant crane presented that program to management.
In Compound, SPC charts were started to track the dry blend transfer time and also Line I and III plasticizer filter pressure differentials. Vinyl started charts on reactor turnaround times.
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VINYL - D. W. Hollis, J. M. Edwards
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Safety
The Vinyl and Yard Departments had one accident which resulted in a sprained knee (first aid).
Shift safety meeting topic for the month was Accident Prevention Off the Job.
Production
March
Y.T.D.(Fiscal 87)
1. Production, MM Lbs. 2. Daily Production Rate, M Lbs./C.D. 3. Total Charges 4. Charges, Reactor Batches/C.D. 5. Reactor Stream Factor 6. Dryer Rate, Average Lbs./Hr. 7. Dryer Stream Factor 8. Accounting Days
34.1 1100
915 29.5 93.3 9816 58.4
31
211.9 1175 5346 29.4 91.1
10306 59.1 182
Vinyl Department production for March was 34.1MM pounds.
Reactors
The reactor stream factor for March was 93.3%. Downtime in the reactor area occurred as follows:
1) Operational Downtime: Accounted for 49.3% of the total downtime and was due to reactor recovery scheduling conflicts, downtime due to rinsing the chem wash tank, waiting on particle size information before charging, reactor manway O-ring failures and downtime associated with test runs and reactor inspections.
2) Maintenance Service Downtime: Accounted for no downtime because the cleaning of the reactor AMS injection ports and inert vent lines was accomplished while the reactors were normally down for other reasons.
3) Maintenance Repair/Revision Downtime: Accounted for 50.7% of the total downtime and was due to changing the agitator seal on D400 and 743, changing various chem wash and rinse valves on 742, 300, 400, 500 and 600, changing the safety disc on 743, adjusting the spray heads on 742 and 741, repair 742 and 745 gearbox oil leaks, replacing the new module Modicon and rebuilding "B" recovery compressor.
Dryers
The dryer stream factor for March was 58.4%. Downtime in the dryer area occurred as follows:
1) Reactor Limited Production: Accounted for 93.5% of the total down time. Dryers were shut down when possible for energy conservation.
2) Operational Downtime: Accounted for 3.0% of the total downtime and was due to centrifuge plugging, burner flameouts, dryer cleaning and transfer activator problems.
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VINYL - Continued
Dryers - Continued
3) Maintenance Repair/Revision Downtime: Accounted for 3.5% of the total downtime and was due to changing out #6 centrifuge, #5 and #7 activator problems, #6 star valve problems, #8 air sweep, air compressor failure, and #7 Sweco motor.
Product Quality Summary
Resin Type
Prime
% of Total "B" "H" Production
5265 5305 5385 5415 5425 5465 Debox Off-Grade Sifter Overflow Pond Resin
Total
2,625,381 3,007,330 15,759,691 9,198,997 2,321,500
(5,380)
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1,073,820
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131,118
7.7 8.8 46.2 27.0 6.8 0.0 2.7 0.5 0.3 0.0 100.0
Quality performance for March was 99.7% customer grade with 0.3% "H" grade production.
A total of eight railcars were shipped as "B" grade during the month which represented 6.0% of the 133 total resin hopper cars shipped.
Load Date Ship Date Car No.
Customer
Product
Reason
02/02/87 02/06/86 02/17/87
03/06/87 RTMX 580088 Western Ag., TX 03/06/87 PTLX 41202 Wexford, WI 03/06/87 PTLX 41609 Capco Pipe, IL
Debox Debox Debox
Quality Quality Quality
02/28/87 03/11/87 PLWX 44279 Vulcan Plast., AL Debox
Quality
03/12/87 02/12/87 3/08/87 3/17/87
03/24/87 PLCX 43861 03/27/87 PLCX 43745 03/31/87 ACFX 52568 3/31/87 VIPX 45891
Capco Pipe, IN Apache Plast., CA Wexford, WI Western Ag., TX
Debox Debox Debox Debox
Quality Quality Quality Quality
The Vinyl area received thirty-two short lead time emergency type orders comprising 11% of the 292 Aberdeen resin shipments in March.
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VINYL - Continued
Monthly Variable Cost Performance
Variable costs for the month were unfavorable at $487.2M resulting from an overall unfavorable price variance of $388.6M and an unfavorable efficiency variance of $98.6M. Resin variable cost for the month was 19.566 cents/lb. versus the budgeted 18.086 cents/lb.
The $388.6M unfavorable price variance was primarily attributed to higher than budgeted pricing for VCM, $432.9M.
The $98.6M unfavorable efficiency variance can be attributed mainly to the unfavorable efficiency variance of VCM, $68.9M.
VCM efficiency for the month was 1.01525 lbs. VCM/lb. PVC versus the budgeted 1.00208 lbs. VCM/lb. PVC.
YTD variable cost efficiency variances in the Vinyl Department totaled $322.2M unfavorable.
Energy Performance/Progress
1. Plant energy performance for March was 2434 BTU/lb.
General
1. Resin raw material in the 0744 account totaled $200.5M.
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COMPOUND - P. J. Kober, J. E. Nickerson
Compound Production
Operating Days
Month
Production (M Pounds)
Average
Operating Day
Fiscal
Rate
Y.T.D.
Line I Line V Line III Total
31 14.5 31
2397 697
4206 7300
77 48 136
14302 4965
23425 42692
Line I operated thirty-one days in March at an average rate of 77M pounds per day. Major items affecting production efficiency were: product changes, 66 hours; quality problems, 19 hours; transfer system problems and maintenance, 15 hours; housekeeping, 13 hours; dicing system problems and maintenance, 5 hours; Banbury maintenance, 4 hours; and running transfer line cleanout to remove streamers, 4 hours.
Line V operated 14.5 days during March at an average rate of 48M pounds per day. Major items affecting production efficiency were: product changes and startup, 39 hours; single-screw pelletizer and hot oil system problems and maintenance, 35 hours; and quality problems, 7 hours. Line V was down twenty-four hours for scheduled troubleshooting and maintenance.
Line III operated thirty-one days during March at an average rate of 136M pounds per day. Major items affecting production were: product changes, 72 hours; dicing system problems and maintenance, 12 hours; feeder problems and maintenance, 9 hours; and running transfer line cleanout to remove streamers, 7 hours.
Quality performance for flexible compounds was 1.3% off-grade of which 94% was due to mill scrap. "BC" production was .9%.
The raw material requirement for flexible compounds was 1.03742 pounds of raw material per pound of compound versus a 1.01122 standard (YTD is 1.01023).
The variable cost variance for compound was $63.5M unfavorable with $2.1M unfavorable due to price and $61.4M unfavorable due to efficiency. The efficiency variance due to product mix was $9.3M favorable. The efficiency variance for compound color concentrates was $17.3M unfavorable due to correction of an accounting error bringing the cumulative variance for colors to $22.7M favorable. The unusually unfavorable overall efficiency variance was largely due to correction this month of an error which last month overstated production by one railcar.
Total compound inventory rose .1MM pounds in March to 7.9MM pounds.
Dry Blend
Month
Average
Operating-Day
Fiscal
Rate_____________Y.T.D.
Production, M Pounds Operating Days
4572 31
147
27133 184
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COMPOUND - Continued
Dry Blend - continued
Dry blend operated thirty-one days during March at an average rate of 147M pounds per day. Production included 80172C, 802736, 90172D, RP-421, 186-139, 223-36, 223-57, 269-12, RP-440, 269-67, 180-31, 269-13, BCF1, 269-123, 269-124, RP-100, and 245-80.
Dry Blend production was hindered by: product changes, 71 hours; delays associated with quality and lab problems and normal Q.C., 56 hours; transfer system problems and maintenance, 14 hours; screener problems and maintenance, 7 hours; and filler system problems, 5 hours.
Quality performance for the month of March was 97.6% customer grade.
The raw material requirement for dry blend was 1.00834 pounds of raw material per pound of dry blend versus a standard of 1.00489 (YTD is 1.00988).
The variable cost variance for dry blend was $25.7M favorable with $15.7M favorable due to price and $10.0M favorable due to efficiency. The efficiency variance due to product mix was $4.9M favorable. There were no major dry blend raw material efficiency variances.
Plasticizer
Production, M Pounds Operating Days
Month
1994 31
Average Operating-Day
Rate
64
Fiscal Y.T.D.
11366 184
Plasticizer operated thirty-one days during March at an average rate of 64M pounds per day. Production included 610P and 108P.
VRP production totaled 165M pounds (8.3%).
The raw material requirement for plasticizer was 1.06392 pounds of raw materials per pound of plasticizer versus a 1.09814 standard (Y.T.D. is 1.10623).
The variable cost variance for plasticizer was $35.1M favorable with $5.7M favorable due to price and $29.5M favorable due to efficiency.
The efficiency variance due to product mix was $2.2M unfavorable.
Quality Improvement
Work on charting process variables continues on all lines. In March, compounders began charting hardness and gravity values on all blenders produced on Lines I and III. These charts will soon be available to customers who have requested them.
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COMPOUND - Continued Energy
Compound Dry Blend Plasticizer
Usage (BTU/Lb.)
Actual
Standard
1830.1 768.0
1675.8
1783.0 730.0
1833.5
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MECHANICAL DEPARTMENT - T. F. Lyon MAINTENANCE - G. A. Morgan, D. A. Miller
There was one Injury to a Maintenance Department employee during the month. A General Mechanic required medical treatment to remove a foreign particle from his left eye. The mechanic was opening the bottom manway on 741 reactor when the accident occurred. An investigation is underway and will be complete in mid-April.
Vinyl
Two reactor seals were replaced during the month. The 400 seal was replaced due to an external leak and the 743 seal was replaced due to an internal leak. The 743 seal had been in service for eighteen months.
Eight reactor valves were changed out and rebuilt during the month.
Both "A" and "B" compressors in the old module recovery system were
replaced with rebuilt spares.
An investigation into recovery
compressor performance and corrosion and erosion problems was
initiated.
The 741 agitator shaft failed during the month. The shaft failed due to bending and was initiated by a notch defect next to the seal mounting flange. A spare shaft was available in the plant.
The following repairs were made to Vinyl unit rotating equipment:
- A new impeller was installed in the new module hot water charge pump.
- The "B" vacuum pump inboard seal was replaced.
- The seal was replaced in the old module condensate return pump.
- The normal kill pump was overhauled.
- The 745 agitator fluid coupling was replaced.
- The input pinion seals on the 743 and 745 agitator gearboxes were replaced.
- The outboard seals were replaced in both 705 and 706 emission recovery compressors.
Dryer Area
Two rotary dryer centrifuges were overhauled during March. Both #6 and #8 centrifuges were changed out and the spare rebuilt. The gearboxes and trunnion bushings were overhauled in both cases.
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MECHANICAL DEPARTMENT - Continued
Dryer Area - Continued
The pond resin centrifuge conveyor was built up and hardfaced with tungsten carbide in preparation for the spring pond resin drying.
The rotary airlocks for the debox screener, #4 and #6 dryer were overhauled.
Instrument and Electrical
The following major I&E work was completed in the Vinyl area:
- A pressure recorder was installed to monitor plant process water pressure.
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- The new reactor unit Gould Modicon PLC was changed out due to a power supply problem.
- New propane leak alarms were installed in the Vinyl control room.
Compound Dry Blend, Plasticizer
The following major work was completed in the Compound area:
- Line I "B" blender gearbox was replaced with a rebuilt spare.
- The Line I product blower was replaced with a rebuilt spare.
- Replaced the #2 dicer spindle.
- The Line V Welex blades were replaced.
The following major work was completed in the Plasticizer area:
- Three sections of corroded cooling water piping were replaced.
- Completed demolition of obsolete piping in P-1.
- The Schenk filter was dismantled for cleaning.
- Extensive repairs to R-l cooling coils and baffles were completed.
Instrument and Electrical
- The Line V single screw hot oil heater was overhauled. The old control system was replaced with an automatic microprocessor based temperature controller.
- The dry blend Titanium Dioxide feeder controls were replaced.
- Additional control room indicators were installed to monitor valve positions on Line V.
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MECHANICAL DEPARTMENT - Continued
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Instrument and Electrical - continued
- Surge protectors were installed on the 110V.relays in the Line V Orbitran to eliminate computer malfunctions.
- The dry blend B&C blender motors were replaced.
Utilities
A new outfall flow recorder was Installed at pond #6.
The boiler steam flow instrumentation was calibrated.
The main breaker at the lagoons was replaced.
The boiler feedwater tank was opened and inspected.
Capital Project Status - R. E. Polk
ABE Nunfoer
Project Title
Status
A5L2
Plasticizer Modernization Phase I
Installation of a cleanout nozzle on the overflow line will be installed by 4/17. Tie-in of the south PA tank will be coDpleted by 4/24, after rfiich the project will be closed to field charges.
C566
Masterbatch Bulk Resin Handling
Pre-shutdown mechanical work is complete. Electrical work is in progress and planned for conpletion the week of 4/6. A shutdown is being coordinated with operations for the week of 4/20.
D5S5
VCM/Propane Gas Detection
All punchlist items are complete. Operational report has been Issued. A field closure notice will be issued by 4/15.
D606
Propane Tank Farm Elec. Revisions
Electrical construction is in progress and planned for completion by 5/1.
D646
City Water Backflow Prevention
Performance of system is being evaluated by process engineering to determine proper operating conbination of well punps and the booster punp. All punchlist items are In progress and planned for completion the week of 4/6.
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Capital Project Status - Continued
AFE Nunber
Project Title
D756
Reactor Jacket Expansion Joints
P596
Reactor Quality Improvements
F786
Resin Quality Improvement Perm. Rigid
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Status
Joints have been placed on order. Delivery Is scheduled for 4/15 on the small joints and 5/15 for the large. BQBrs for Installation have been issued. A pre-bid meeting will be held on 4/7. Bids are due the week of 4/13.
Have experienced scan time problems with with the VCM meters. Engineering is working on solution.
Design for the new module Is 50% oouplete and In progress. Installation of the old module is planned for oonpletion by 6/1. The new module work will be coordinated with the annual turnaround planned for October.
Phases I and II engineering are to be oouplete by 4/15. Bids have been received for Phases 1 and 2 electrical scope and are being evaluated. A contract has been awarded for the mechanical portion to Sunland, Inc.
Contracts - C. A. Clark
A total of five construction contracts and forty-five register tickets were issued during the month of March.
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PROCESS ENGINEERING - V. E. Messick
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Resin Quality Improvement Project
A. Flexible Resin Technology - A report was Issued on the third experimental design that quantified the effect of colloid charge volume and use of BPA versus AMS killed recovered VCM on particle size. Alcotex testing showed that the final cool down temperature did affect particle size and established the need for more cooling capacity in summer months.
Investigation into high hard particle results showed high dryer inlet temperature spikes increased hard particle counts. Operating procedures have been revised to reduce these, high temperature spikes. Samples were sent to RAD for analysis. R&D and plant personnel tested several options to reduce foaming and hard particles with the goal of increasing batch size. Only post pressure drop Alcotex injection was believed to be successful. Work is currently underway to revise the reactor interlock logic to allow this injection. Modifications to four reactor rinse sprayheads proved successful in reducing wall scale.
B. Rigid Resin Permanent Facilities - A partial AFE to cover initial engineering to design the permanent suspending agent make-up and charge facilities for production of the new flexible resin has been approved. This scope of work was given to Litwin to design along with the permanent rigid resin facilities. Preliminary layouts of the make-up and charge building were completed by the plant. These layouts were reviewed with PED, GED, and Litwin. Visits by the agitator vendors to observe colloid make-up were scheduled and are underway. Review of equipment inquiries for the permanent systems has begun. Construction of the Polivic system for D-700 reactor and the dump system for D-745 reactor has begun.
C. RQIP Environmental Team
The organic loading estimate was revised during the month to reflect changes in projections of new technology formulations. A sampling plan was proposed by Tom Heller, PED, to gather sufficient data for a mathematical model of the plant's wastewater system. The model will be used to predict the wastewater system performance with increased organic loading from the new technology.
PCB Removal Plan
A letter outlining the scope and specific steps to remove all PCB equipment was issued and reviewed.
5305 Antistat Testing
Two new antistat agents (Atmer 129 and Span 20) were tested on 5305 to determine if fusion characteristics improved over calcium stearate coated resin. Both controlled static at acceptable application rates and appeared not to be detrimental to fusion characteristics.
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PROCESS ENGINEERING - Continued
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Vinyl Area Distributed Control System
Work has begun to determine the scope, justification and cost of installing a distributed control system in the vinyl area.
Dry Calcium Stearate Addition System
An additional test was conducted on the fluid bed dryer during the month. The review issue of the class "A" design was issued and a review meeting held. The AFE request with economics was completed and submitted.
Line V Operation Consistency
Production on Line V was monitored during the month to determine the causes of inconsistencies experienced at customer accounts. Several revisions were recommended and implemented based on operating problems found. A report is being prepared.
VCM/Recovery System Seal Water Filters
As part of the TCLP study, the existing systems are being investigated to determine ways to reduce the VCM level so the filters will not be classified as hazardous. Recommendations have been made to revise systems to allow for more thorough stripping.
Reactor Slurry Containment
As part of the TCLP study, all systems containing reactor slurry were surveyed to determine potential for spills. Recommendations were made to provide additional curbing, process drains, and concrete area to contain spills if one should occur.
Compound Fusion Team
Team members attended the CTCC meeting held in Aberdeen on 3/19. The team's
objectives and planned action steps were presented at the meeting. The team
formulated an overall objective list; distributed this list to all parties
present at the CTCC meeting including Premiere and Blane Polymers for input.
Team members are soliciting input from all parties on variables that could
significantly
fusion. This input will be used to formulate
experimental designs in April. Preliminary results of testing with the Very
Simple Test (VST - pressed plaque test) indicates that this test can
distinguish between material produced at different stock temperatures for
35852. Validity of the test will be checked with different hardness
compounds produced at a series of stock temperatures.
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VAB.0001191431
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PERSONNEL - R. A. Miller
EMPLOYMENT Arthur J. Stewart, New Hire Jeffrey Popp, Co-op Student returning to work
PROMOTIONS/TRANSFERS
Keith L. Fogg, Safety Director, LAB Plant, to Safety Director, Aberdeen Plant
Jack E. Little, Office Manager, Premiere Polymers, to Director of Administrative Services Chris Gilreath from Compound Utility to Vinyl "A" Operator Larry Brown from General Helper to Vinyl "A" Operator Donald R. Whatley from General Helper to Compound Utility
RETIREMENTS None
TERMINATIONS Charles E. Morris, deceased W. F. Higginbotham, employee resigned Thomas A. Madigan, Co-op Student returned to school
TO/FROM LEAVE OF ABSENCE None
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VAB.0001191432
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Aberdeen, Mississippi
A
Salaried Employees
Hourly Employees
Total Employees Employees (Hourly)
d
New Employees
Terminations
74** 168
0 0
DEPARTMENTS PAR # EMPLOYEES
Warehouse Gen. Plant Maintenance Laboratory
14 16 39 22
16 13 38 24
Compound Vinyl
33 32
40 32
Plasticizer
4
5
MARCH MONTHLY PERSONNEL REPORT
Minority Employees #
0o
Salaried Hour1y
8
65
ill 39%
Total
73 30%
EMP 7
6 8
5
Hourly Min. Hired % Min. Hired
Hourly Min Term. % Min. Term.
0
0 0 Q.
% MIN.
AA
NEW HIRES
4
0
YTD 0
TERM. YTD TURNOVER 00
46 0
7a
a
0 0a
a
0 ._
0
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YTD a
28 9
m 28
0
___________________________
____________________________________
_Q_
___ 0_______
Q
a
a
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40 0
0 00
o
o
Number of Applicants:
Month
*
2 Year to Date
APPLICANT BREAKDOWN:
# Minority
i
% Minority
^ Female
i_____ % Female
7
50 so
Hires (Hourly) :
Month
0
Year to Date
Terminations (Hourly) :
Month
1 Year to Date
Overal1 Turnover
. 6%
Projected Annual Turnover
7 2 2.4%
* Includes 1 temporary employee and one Co-op Engineer.
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O V E R T Itt AND ABSENTEEISM
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ENERGY CONSERVATION - F. G. Jeanson
I. Plant Operations
Total energy consumption for March was 116.861 MMM BTUs. Energy consumption decreased to 2434 BTU/lb. from 2444 BTU/lb. In February. An adjusted CMA reduction of 52.3% was obtained for the month. The adjusted CMA reduction for fiscal 1987 Is 53.9%.
II. Plant Energy Conservation Program
A. Maintenance
There were twelve energy related Items completed In March. Nine of these Items were steam leak repairs. The remaining three were steam trap repairs.
III. Boiler Operation
Boilers
No. 1 No. 2 No. 3
Combustion Efficiency %
March, 1987
March, 1986
(1)
83.4
83.1
83.7W
83.7 83.6
Note: (1) Boiler number one was not used during the month. Boiler number one was operated three days during the month.
A
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VAB.0001191435
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Month
ENERGY CONSERVATION DATA 1987
March
Production, MM Lbs.
Resin Dry Blend Compound Plasticizer
TOTAL
34.1 4.6 7.3 2.0
48.0
Natural Gas
Consumption, MSCF Conversion, BTU/SCF Energy Consumption, MMM BTU Energy Consumption, BTU/lb.
56681
1020
57.815 1204
Electricity
Consumption, MM KWH Conversion, BTU/KWH Energy Consumption, MMM BTU Energy Consumption, BTU/lb.
*
5.9046
10000
59.046 1230
Propane
Consumption, M Gal. Conversion, BTU/Gal. Energy Consumption, MMM BTU Energy Consumption, BTU/lb.
0
92000
0 0
Total
Energy Consumption, BTU/lb.
2434
Energy Consumption, MMM BTU Actual Unadjusted Actual Adjusted 1972 Base Period
116.861 96.774
202.933
CMA Reduction (%)
Adjusted Unadjusted Fiscal 1987 Year-to-Date
Performance
53.9% Adjusted 44.2% Unadjusted
52.3 42.4
1986 March
38.7 3.9 6.0 1.3
49.9
*
61191
1020
62.415 1250
5.5884
10000
55.884 1120
0
92000
0 0
2370
118.299 89.216
214.347
58.4 44.8
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VAB.0001191436
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ENVIRONMENTAL - F. G. Jeanson
Water
One minor wastewater violation occurred on March 19 when the pH of outfall 003 was measured and found to be 9.7. The current limit is 9.0
All other wastewater discharge parameters were within NFDES limits during March.
The quarterly bioassay sampling was completed.
EPA laboratory performance samples were received and sent to EnviroLab. Results will be returned to EPA in April.
Waste Management
One truckload of waste oil was shipped to Stauffer Chemical Company.
One truckload of drummed waste (filter cake and paper, stabilizer spill, PA spill) was shipped to Chemical Waste Management (CWM).
Eight dump truckloads of vacuum dust were shipped to CWM. All vacuum dust that had collected at Prairie over the past year has now been removed.
One dump truckload of Line I construction sand and concrete was shipped to CWM.
One truckload of reactor culls was shipped to Sun Polymers.
Reporting
The quarterly NESHAP report was completed and issued.
An amended underground storage tank notification to the State was issued.
A pollution cost survey for Tom Roberts, Accounting-Houston, was completed.
A
..............................................................
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TABLE I WATER QCMPLIANCE WTffl NFDES PEFMTT PARAMETERS
A
Oct. - Ave. Max.
Nov. - Ave. Max.
Dec. - Ave. Max.
Jan. - Ave. Max.
Feb. - Ave. Max.
-
Mar. - Ave. Max.
Apr. - Ave. Max.
May - Ave. Max.
June - Ave. Max.
July - Ave. Max.
Aug. - Ave. ttex.
Sept. - Ave. Max.
flow GEM
1010 1207
1031 1075
987 1350
1062 1300
858 900
903 970
BCD PEM LB./DY.
6 77 10 120
15 183 17 213
23 268 46 373
15 194 20 310
14 142 26 266
11 119 21 217
OGD PEM LB./DY.
26 311 33 404
33 406 42 527
71 846 110 1284
53 662 57 775
42 431 75 766
38 409 50 541
Sus. Solids PEM lb./dy.
14 165 23 281
23 281 37 464
13 179 24 302
18 231 28 434
10 99 13 140
19 206 35 362
Dias. 0^
7.4 8.0
8.2 9.1
7.6 8.6
9.6 10.3
10.0 10.6
8.8 10.5
NH_ LB./ny.
2.7 7.3
0.1 0.1
2.0 4.7
2.1 4.6
4.9 9.3
4.0 7.6
pH
7.6 8.0
7.6 7.8
7.3 7.8
7.7 7.8
7.7 8.0
7.8 8.3
NEPES Permit limits - Decenber 1 through April 30
Ave. Max.
32 431 43 800
- 1462 - 2713
NPDES Permit Limits - May 1 through Novenfcer 30
Ave. Max.
26 357 40 744
- 1212
- 2523
674 13%
> 6.0
13 6.0 - 9.0 28
674 13%
13 6.0 - 9.0 28
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LABORATORY - H. G. Coleman/J. R. Williams
Safety A. Safety
There were no recordable first aid or medical cases for the month. One employee was placed under observation when he suffered a slight muscle strain in his back while lifting a fifty-pound bag of resin; he has fully recovered.
B. Customer Relations
Customer Contacts
Hoechst Celanese - H. G. Coleman accompanied Research and
Marketing personnel to this customer on March 4 to discuss
quality control testing and correlation of results for 5305.
We agreed to help him i(kRuussss Rxnhooaaads); set up his new HS-100
headspace analyzer and subsequently sent him our test method.
Once his machine has lined out, we will arrange a sample swap
for a correlation study. Multiple samples from a 5305 railcar
were analyzed for I.V. and RVCM in response to one of their
queries on consistency. Little variation was
a report
was issued on 3/31.
AT&T - A. Kelson of AT&T, Omaha, visited the plant on 3/18 to discuss the elimination of the QMS inspection system and accepting Vista in a Vendor Partnership arrangement. A report was Issued on 3/23 outlining our proposed Q.C. testing of their jacket compound.
Donnelly - Representatives from this automotive glass manufacturer visited the plant on 3/26. The main areas of concern were in SPC (they want us to send them data) and melt flow, a test they feel is important in characterizing compound properties. A plan will be written addressing these issues.
Polytex - B. J. Harrison visited this customer on 3/10 to investigate complaint of color and processing of 223-204 White 144. Subsequent testing at Aberdeen and Ponca City could not verify a problem.
Viceroy Homes - B. J. Harrison visited Viceroy on 3/11 to ascertain their preferred shade of beige (BGE 349 not acceptable). Color match was achieved by Americhem and a pilot sample was prepared in Ponca City, 269-168 BGE 320.
Eaton - G. Siler visited the plant on 3/10 and conducted a Vendor Q.A. Survey. This was last performed by Eaton in May of 1985. There were no major issues brought to our attention.
Requests for Corrective Action
There ware no RCA's received In March.
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LABORATORY - Continued
Customer Problem Reports
Date
Customer
Product
Reason
3/03 & 3/13 Flexible Technologies Abbeville, SC
17121 CB50
Large gels Chard particles) in finished hose.
3/03
Bolytex Gakmont, PA
223-204 WKT 144 Material causing high torque and is off-color (too white).
3/04 3/20
Southwire
urc
Lithonia, GA
5425 5415
Wasps In top of railcar.
Steam evolution (moisture) from pre-blend Intensive mixers.
Waivers Issued
Customer
Product
Reason
No.
Colby Plastics 80172C
Fusion & Eq. Torques
1 RC
Hayes Dockside 5265
Moisture
1 RC
Hayes Dockside 5305
Static Flow
1 RC
Nibco
5305
Static Flow
7 HT
mal Industries KP100 Wit 141 Color
17 Baxes
Uniroyal
5305
Static Flow
1 HT
C. Development Lab Summary
The following is a summary of residual VCM results on in-process samples. None of the reactor daily averages exceeded 400 ppm during the month of March, 1987.
Reactor
________ Drier
Slurries52655305
Nunfcer of Samples Average ppm, VCM
911 204
44 3.0
60 0.7
RVCM of Shipment Sanples
The following is a summary of the residual VCM analysis of shipment sanples for the month of March, 1987.
Product
5265 5305 5385 5415 5425 5465 Debox Dry Blend
No. of Samples
22 86 39 35 21
Average RVCM, ppm 1.1 0.3 0.5 0.1 0.2
4 28 0.1 0.4
26 0.3
.
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VAB.0001191440
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LABORATORY
D. Resin Process Capabilities (CFK) - Regular (Dryer) Sanples
Bulk Density
5265 0.64
5305
& 0.09
5385 2.63
5415 1.85
5465
Inherent Viscosity 0.52
0.74
0.77
0.61
"L" Color Value
1.60
4.75
4.22
4.11
"A" Color Value
1.44
4.17
--
--
"B" Color Value
% on Fan (vs. 2% max.)
% thru 140m
1.00 1.38
1.11
0.78 5.00
2.04
1.67 4.00
2.14
3.67
No
Production
2.17
(0.50)
-
1.36
Drytime
--
--
0.67
0.83
Mets IR (vs. 95% of control)
**
1.35 (0.69)
Hard Particles (% y 10)
--------- ----------
13.9
20.1
* 5305 bulk density CPK is unusually low due to elimination antistat from dryer outlet (to satisfy Hoechst Celanese).
E. Compound Quality Summary - M Lbs.
Adjustments (%)
Rejections (%)
Hardness Color/Clarity Hard Particles
15.0 (0.21)
0.0
(
-
)
0.0
(
-
)
10.5 0.9
55.3
(0.14) (0.01) (0.76)
Heat Stability
7.0 (0.10)
3.6 (0.05)
Dispersion Dicing Streamers
0.0
)
(
-
0.0
(
-
)
0.0
(
-
)
24.9 18.1 21.0
(0.34) (0.25) (0.29)
Total
22.0 (0.30)
134.3 (1.84)
A
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LABORATORY
F. Dry Blend Quality Summary - M Lbs.
Rejections (%)
Color
90.8
(1.99')
Color/Fusion Torque
9.4 (0.21)
Total
100.2
(2.20)
6. Miscellaneous
1. All laboratory personnel attended the "Problem Solving and 4 Involvement Teams" training program given by our on-site QDC,
Rendell Newton.
2. TCLP Testing - The first samples were shipped to both the LCCP and to an outside lab (ETC). Also, equipment was placed on order that would allow in-plant TCLP testing to be done.
3. Work was begun on converting an existing steam-heated roll mill over to an oil-heated system. A miscellaneous project was approved on 4/1 to purchase and install an oil heater. This will allow dry blend color Q.C. to be performed in a non-plasticized formulation and at temperatures more closely approximating the end user.
4. Discovered a wetness/clumping problem with the new PMS blue
colorant 30389T.
Material was used successfully after
screening by production, but with a 50% loss of raw material
and considerable overtime expenses. The supplier was contacted
through Purchasing for retribution.
VAB.0001191442
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ADMINISTRATIVE SERVICES - PAUL RIESENBERG
SHIPMENTS BY PRODUCT - M LBS.
Resin Plasticizer Dryblend Compound
MARCH 1987
29,591 1.024 5.025 7,587
NUMBER OF SHIPMENTS BY MODE:
OT
R/C BULK
TOTAL
OT VAN
43,227#
TOFC
CC
A
FISCAL YEAR-TO DATE
164,758 4,445
27,460 42,632
239,293#
CPU CN TOTAL
October November December January February Ma re h April May June July August September
116 146 133
193 154 181
41 51 64 39 46 29
68 44 50 45 60 56
2 2 1
3 3 0
CPU AIR CN TOTAL
52 160
422
64 135
450
48 133
390
89 147
544
55 143 1
451
64 129
3 493
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ENERGY USAGE
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MONTHLY HOURLY TURNOVER
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=r*mn-
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1r'
H-nil
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VAB.0001191446
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ire a-'-'-il I- L- . Ji *C-j-|jdL ,!- <!-. .-.| .1-1 -1-f
C-
V- '
6.0 5.0 4.0 3.0 2.0
1.0 [
0
%
OFF-GRAD?
1
V
ABERDEEN PLANT QUALITY PERFORMANCE
10/01/86 - 09/30/87
A
4.0 3.0 2.0
1.0
0
Oct.
Dec.
Jan. Feb. Mar. April
iq 86/87
June
..:r *;.
..'.pl-r...-.1 ^
1,1 ! |l L. L
:i
. ^>| |;|q:=.-F '\*5i J i^*l
m (?! M Th-.-n|^>p-1| TTT^Jli%tt^F^>i
Sept.
VAB.OOOl 191447
mwv<r^=Kiflp <
jutn.. .UUw.&.
MM POUNDS
PRIME
ABERDEEN PLANT INVENTORIES
10/01/86 - 09/30/87
*P
if
.1.1 !1- > +-T !> J+r: c:ipv--j`H* \ J:.: it . 4i< .. . H
|+ ^(Udrtr
- t+qVrti fe*
i-*p h*`i
t i -rfiTrtar^'
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*
VAB.0001191448
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vy.*-
-:| ,-vuc. | r.A liqt-.H'i .'^iHitoi^TT
r MM POUNDS V MONTHLY
40 35 30 h 25 20 15
ABERDEEN PLANT PRODUCTION
10/01/86 - 09/30/87
A
MM POUN
-.mi || i ,i IHfthI
8
6
4
2
6
5 4 h3 2
1
2
1
0
Oct.
Dec. i Jan.
I-tH--InhBrfcfc- Im^ji .
-'.t IH...-J.IIL'- .1*
-1411
inwnwwumww<I* ij
Mar. April! May
O
June
Budget Actual Cumulative
, i,.. wimhi.in^
i -i-.
r
20
15
10
5
Sept.iOct.
4
VAB.OOOl 191449
ABERDEEN PLANT EFFICIENCY
10/01/86 - 09/30/87
A
1.200
1.190
1.100
1.050
Oct. Nov. Dec. Jan. i Feb
Mar. Apr. May |June July
19.86/87
'ayt'.y -
I-.4H-IL.
hl-H
T+
-'i* ir '--m'Ttriri minim ...............waaim ..mh
VAB.OOOl 191450
r iri* . i1 '