Document v6kg8pDVZpbKGMdgxkkXR6Jnb
W. R. Bailey - Delaware City S. BrouMlar^ D. E. Frey V. Hehle/WT"u. Hutton - Pasadena R. Henderson - Independence D. L. Lull R. J. Sutch - Cleveland J. E. Zimmerman - Cleveland D. P. Tech. File 16.17.(b) File 712L
May 24, 1978
Mr. Richard Miller Industrial Hygienist Occupational Safety and Health Adm. 2320 LaBranch Street Houston, Texas 77004
Dear Mr. Miller:
Attached is the additional information you requested during your inspection of our Deer Park PVC Plant on May 18 and May 22, 1978. Exhibit numbers have been included for each reference:
Exhibit I Exhibit I I
Complete report of May 18, 1978, VCM spill.
VCM releases for last nine (9) months involving personnel exposure.
Exhibit i I I Exhibit IV Exhibit V
Description of VCM monitoring system.
Corrective action for missing valve handles.
Personnel sampling data for last six (6) months in general area where spill occurred.
Also, you asked about the source of our monitoring equipment. The vendor who supplied the equipment for our continuous monitoring system is Areas, Inc., 8500 Commerce Park Drive, Suite 110, Houston, Texas 77036, and their phone number is (713) 777"2392.
If you have any additional questions or comments, please do not hesitate to contact us.
Sincerely,
(c^JLv^L P*
RPB:Imr Enclosures
Rodney P. Becker Plastics Plant Manager
OCC 11097
Diamond Shamrock Corporation P O. Box 600, Deer Park, Texas 77536 Phone, 713476-2C00
EXHIBIT I
INTRODUCTION
Polyvinyl chloride is made by polymerizing vinyl chloride monomer. In the initial charging operation, water, catalyst, suspending agents and vinyl chloride monomer are manually charged through meters to an agitated pressure vessel where they are then heated to initiate the reaction process under controlled conditions.
LOCATION
The #4 Plant process area where the spill occurred contains ten (10) 2000 gal. reactors and allied equipment such as charge pumps, instruments, piping, and compressors.
The #3 Plant process area just South of #4 Plant and adjacent to #4 Plant con tains the same inventory of equipment. The manpower required to operate these process areas include a total of nine (9) men. These men are engaged in the charging, dropping, cleaning of the reactors and for the drying of the finished product. The personnel responsible for the drying area are also required to monitor the operation of the charge pumps, compressors, and other equipment located in the ground level area since the charging operation takes place on the second level.
INCIDENT
On the morning of Hay 18, 1978, an operator who was in the process of charging #44 reactor had completed the addition of all of the raw materials except the vinyl chloride monomer and was pulling a vacuum on the reactor prior to the addition of the VCM. (The reactor evacuation process is a standard operating step in the reactor charge procedure.)
When the desired vacuum was reached on #44 reactor, the operator proceeded to open the VCM valve and meter the VCM to the reactor. Standard operating pro cedure for this step is to close the evacuation valve and then open the VCM valve but for some reason the operator failed to -close the evacuation valve.
EVACUATION
Evacuation of the reactor is done via a Nash water sealed compressor that pulls the reactor vapors from the reactor and discharges them to a gasholder collec tion system where they are later condensed and returned to the process. The seal water for this compressor is recycled through a small tank which is an allied part on the Nash compressor. Since the VCM vapors that are being re moved from the reactor are laden with water, a level controlled dump valve s installed on the seal water pot to control the water level. When the water level gets high, the dump valve opens and discharges this water to a process sewer.
SPILL
When the operator failed to close the evacuation valve on the #44 reactor, the liquid VCM that was being charged was carried into the evacuation compressor and compressor seal water pot. The automatic dump valve then opened up to re duce the seal water pot liquid level and discharged the liquid VCM to the open process sewer.
OCC 11098
SPILL (Cont'd)
Operating personnel in the Number 3 and process areas immediately rushed to the compressor area to isolate the spill by closing the suction and discharge valves at the compressor.
A diagram of the poly evacuation process is attached to this report.
THG:lmr 5/19/78
Ted Guth
OCC 11099
\ ] ! i :i
I i
o Q
i
Q
O O
i
Diamond Shamrock
EXHIBIT II
bcc:
L. G.
.son
N. F. Fahnoe
T. 0. Isbell
November 29, 1977
Mr. Ronald McCann Safety and Health Director U. S. Department of Labor 2320 LaBranch Street Houston, Texas 77004
(OSHA)
.
Dear Mr. McCann:
At 11:51 A.M. on Novemher 26, 1977, a VCM release occurred at our Deer Park Poly Vinyl Chloride Plant as a result of metal fatigue to a screen pot stud bolt which allowed the screen pot lid to blow off and discharge water, PVC and residual amounts of VCM vapors to the atmosphere.
The total time of the emergency was estimated to be 30 seconds and the highest reading recorded on the Personnel Monitoring System was 861 ppm of VCM.
There were two (2) operating personnel who stated that they had smelled VCM during the release and they were sent to First Aid for medical examination. Neither one of the operators were wearing respiratory protection. Operators involved were Rudy Ybarra and Mike Mulkey.
The VCM .release amounted to 184 lbs./VCM.
Events leading up to the release are as follows:
An operator, Rudy Ybarra was in the process of discharging a finished batch of PVC slurry from It51 poly (which is located in our It4 Plant Expansion Area) through the screen pot and into the blowdown tank. The screen pot lid blew off releasing water, PVC and VCM vapors to the atmosphere. Mike Mulkey who heard the noise caused by the release immediately rushed over and closed the drop valve on the poly. A VCM sensor located approximately six (6) feet from the screen pot detected a concentration of VCM and sounded an alarm located in the Poly Control Room.
Corrective action to prevent personnel exposure from releases occurring at the screen pots will include the isolation or closing of the drop valve and the evacuation of the affected area by all personnel.
Sincerely
DIAMOND SHAMROCK CORPORATION
RPB:lmr
Rodney P. Becker Plant Manager
OCC 11101
Diamond Shamrock
D. E. Frey DA. Lull Rn ^^l. cS.u. +tc,,h D. P. Tech. File 16.03-b(1)
May 18, 1978
Mr. Richard Miller Industrial Hygienist Occupational Safety and Health Adm. 2320 LaBranch Street Houston, Texas 7700^
Dear Mr. Miller:
At 0511 A.M. on May 18, 1978, a VCM release occurred at our Deer Park Polyvinyl Chloride Plant and seven (7) of our employees were exposed to VCM. The highest level recorded by our monitoring sys tem during the release was 971-3 ppm/VCM. All of the employees exposed to VCM were examined by our First Aid Department and no ill effects were reported. The names of the employees exposed are as follows:
L. Singleton J. Davis L. Verrette R. Corpus
B. Byous E. Lujan J. Jonas
The total amount of the release is estimated to be 380 lbs./VCM and was a result of an operator error. The operator involved was in the process of charging a reactor in our 8h process plant. During the charging operation he failed to close an evacuation valve on the reactor before commencing to charge the liquid VCM.
The liquid VCM escaped through the open evacuation valve to the water sealed Nash compressor. The dump valve on the Nash seal water pot then discharged the liquid VCM to the process sewer.
In their haste to isolate the spill, none of the employees wore respiratory protection although each employee is provided with approved respiratory equipment.
Sincerely,
RPB:lmr
Rodney P. Becker Plant Manager
OCC 11102
Diamond Shamrock Corporation P.O. Box 500, Deer Park, Texas 77536 Phone 713 476-2000
Diamond Shamrock
October 21, 1977
Mr. Ronald McCann Occupational and Health Administration Room 2118 2320 LaBranch Street Houston, Texas 77004
Dear Mr. McCann:
On October 21, 1977, at 0920 hours a VCM release occurred at our East Poly vinyl Chloride Plant in the monomer recovery area when a safety valve blew on an accumulator.
The VCM release was caused by a mechanical failure of the high level alarm on the reclaimed monomer pump-back-tank normally referred to as the accumu lator.
Two operators, Mr. Lonnie Follis and Mr. Melvin Eudy, who were near the scene, immediately shut down the reclaim compressor, but were exposed to an undetermined amount of VCM during the process. Neither one of the operators were wearing respiratory protection.
Both of the employees reported to First Aid for medical examination with no ill effects reported.
The VCM release was calculated to be 658 lbs./VCM and total time of the emergency was two (2) minutes. The highest concentration of VCM recorded by our continuous monitoring system was 38.9 ppm.
The accumulator level alarm was repaired before the recovery system was put back in operation. The relief valve discharge stacks will be elevated to avoid future employee exposures in case of an emergency relief valve discharge.
Sincerely
DIAMOND SHAMROCK CORPORATION
EZ:lmr bcc: L. G. Davison
N. F. Fahnoe VJ. C. Hutton
'T't rt T -- L ~ 1
^. ;r. teen, rile I6.03b(i)
P"irr*n'^
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E. Zinn Plant Manager
Pc'.'' C'rvL Too' 7[H-.
OCC 11103
-nnn
Diamond Shamrock
August 23, 1977
Hr. Roy Piggee Occupational and Health Administration Room 2118 2320 LaBranch Houston, Texas 77004
Dear Mr. Piggee:
On August 22, 1977, at 2347 hours, VCM vapors were released to the atmos phere when a 3/4" plug blew out of a monomer recovery compressor.
The monomer recovery compressor is operated in intermittent service and had just been put on-stream. The operator who was at the scene, immediately shut down the compressor, but was exposed to an undetermined amount of VCM during the process as he was not wearing respiratory protection.
No ill effects to the employee occurred as a result of the exposure and the employee reported to first-aid for medical examination.
The VCM vapor release was estimated to be 5 lbs./VCM and the total time of the emergency was two (2) minutes. An L.E.L. (Lower Explosive Limit) sensor detected the VCM vapors and tripped our recovery area sprinkler system as added protection.
No high VCM readings were recorded on our continuous monitoring system during the time of this emergency.
The plug was replaced in the compressor and normal operations were resumed.
Sincerely,
DIAMOND SHAMROCK CORPORATION
EZ: lim
bec : cof'i ^
L. G. Davison N. F. Fahnoe W. C. Hutton T. 0. Isbell B.rjp.' Tech File 16.03.b(l)
E. Zinn Plant Manager
OCC 11104
Diamond Shamrock Corporation PO Rr S00 Park
7753n Phnnr* 713 **76-?000
ARCAS VCM MONITORING SYSTEM
The Areas System is basically a communications system. It sequentially analyzes 80 designated sample points strategically located throughout the Plant on five separate G.C. Units. The most recent analyses from the five systems (No. 1, 2, 3, & 5 Plants) are stored in the multiplexer. The multiplexer scans all data sending out the most recent information to the Environ mental Head Operators deewriter and to the remote warning stations if an exposure is imminent. Each time the next higher level is exceeded, a visual light is displayed. The primary function that the system serves is to feed back VCM concentrations and designate respiratory protection to be used by way of the remote exposure warning stations the operating areas and the personnel in those areas. Action levels displayed at the designated warning stations are 5 ppm (white), 25 ppm (blue), 1000 ppm (yellow), and 3600 ppm (red).
If a warning light is displayed and respiratory protection is not available, you must IMMEDIATELY LEAVE THE AREA.
TMG:lmr 5/11/78
OCC 11105
ANALYTICAL EQUIPMENT
ARCAS INC.
*>Ofi CQHMCnCE f'AHK DU., SUITE. I IO
HOUSTON. ttXAS 1713) J7
PROGRAMMER DATA SHEET
Customer Diamond Shamrock
Date 'December 1D75
Address Deer Park, Texas
Job 4^ 5X1054 Type of Mount:
p.O. # H95368-7 ' Model
505D FID
/ / Panel
/ / Rack
/x/ Field
Electrical Classification: / / General Purpose
/x/ Explosion Proof
Cycle Time: Tuner:
i minutes
/x/ S. M. Digital
seconds
Count Rate
one second
No. of functions (slots)_______7
Function slots not used
2
/ / Cramer Cam Motor Speed Gear Rack_
No. of Cams
______.
No. of Cams Not Used
/ / Other
________________
Number of Streams_______^_________ / / Manual Switching
/x/ Automatic Switching
Detector Current No. of Attenuators^ Notes:
_ma. (T.C. units only)
/ / Dual Range
OCC 11106
* nmicirwi rC
IMP
Timer Functions 1A End of cycle -
2A Auto zero 3A Column switch 4A Peak One 5A 6A 7A 8A 9A 10A 11A 12A 13A 14A 15A loA 17A 18A 19A 20A
inject
Time
060
024
058 027
`
IB Sample block 2B 3B 4B 5B 6B 7B 8B . . 9B 10 B 11B 12 B 13B 14B 15B 16B 17B 18B 19B 20B
Time 057
020 039
Components__________ Attenuator #
Vinvl Chloride
1
Streams 1-16
Range %/ppm 0-3.6%
Notes
A DIVISION OF ANACON. INC
OCC 11107
JOB # 5110
VALVE #1
Sample valve type 6 port s ,s .-l/8"-Arcas slider__________________________
Sample loop
External_____________ Length 6" x 1/8"
Volume
Carrier gas
Helium^ Bottle regulator
50. PS I
Carrier pressure
Reg 1 ^30 psi
Reg 2
23FSX
Column, configuration Precut with backflush to vent Precut column 1' chromosorb 102 80/100
Analytical column 2' chromosorb 102 80/100
Other
Flows;
measured with bubble tube
Reference
cc/m Column
cc/m Backflush
45 cc/m
VALVE #2
Sample valve type
Sample loop ' Length _________________________________________ Volume ______________
Carrier gas Bottle regulatorPSI
Carrier pressure
Reg 1 PSI
Reg 2 PSI
Column configuration
Precut column- _*
Analytical column
Other _.
FI ows : measured with bubble tube
Reference cc/m Column cc/m Backflush __________________________________cc/ii
BOTES:
_____________ ______________________ CC Uio8
Model # 905 Separation of
Job #*511054 vinvl chloride from air
Oven type
Air Bath
Field electronics /x/ Purged
(check one)
J Condulet
Detector type_______FID
F.I.D. Units only -- Bottle regulators supplied by customer-
Zero hydrogen bottle;
;*
Pressure setting 40 PSX Flow________________60___________ cc/rg
Restrictor type fixed capillary
Zero air bottle r
Pressure setting
40 PSI Flow__ 300
cc/nt
Restrictor type __________________variable needle valve
Instrument air pressure:..
Source
50 PSI
Oven air pressure 40 PSI setting
Operating temperature
230
Temoerature controller
zero crossing
Check one / / Plug Card
fa / Gup Mounted
Temperature probe
__________thermistor 1 meg 250 C_________
High Temp. Cut-off Switch
standard on all units/set at 300F
Carrier Protection
standard on all thermal cond. units
Power Switch
/ / yes
.hJ no
OCC 11109
EXHIBIT IV
DACO Z7
t
MEMORANDUM
To /<>/ //______________________________________ Subject //U/. l/ZZ /-/zl/ZZZZ
Date Z5~~ j3S- *7&
V//-T /S T'O Z?0A//r//?sr7 -7-ZS/27' Z^t>2T/g^ i^ZlZ^ &/sZ /ZoZ <S ZAL___ ^ - 4- - 4r>Z___ ,4^Z___# AZ/P/ZZJZZr
-Z77
- < /?7sOD<^ t~A//S ZTA/ZT/^tTcZT'/ZZsy
/y^f^r/A"__________________________________ _________________________
occ lino
M?}/33, /<?'/&
'1 -7&. /_________^/r/Z
'i
______________
,'Jv30/?7.^._______/-/?/?___ __________________ ,,________ ___________________ _______
____r/oM_ (3-4- 4*^
j
I___ ,,/Al--JMA/Lr- ^_____________________ k'tfJ- t/'---_///jA/0<L3.
t
____ /A/S33C-T/&M
/MC0/?ro/?& TcLD s/S ~T/43.
___ /77&/vr// .../,&/?/' fhr/z&t /a/3/30r/6W...........................
____ 0<0S
^rd:td>/j!3fc<Z-.....________
____^r/A'^tyV^Z y/r/,2*7S,.. (4-)
........ tf/C/?. d?/?S3(0^________________ __ ___
occ mu
DAH:
\/2\//'7 2/1 4/ /7 tl /04/ /8 iR/09/ / 8 ).i/02/ /8 M/03/ / 8
DEER PARK PLASTICS VCM CEILING EXPOSURE
J 08
3-4 DRYING 3-4 DRYING 3-4 DRYING 3-4 DRYING 3-4 DRYING 3-4 DRYING
NAME
J. VALENZUELA D. HERNANDEZ R. MURPHY T. CASKEY R. MURPHY D. HERNANDEZ
TIME DESCRIPTION
15 15 15
320 15
1b
OPEr. dryer ort ITCHED BIN.) HOU11 NE DUTI ES
iiASHED DOWN routine dry. oAMPLED,Toner #s
vcm
0. 49 0. o3 0. 7 4 0.28 i . 53 0. 54
DA; L
i /os/ n
1 /' 3 0/ 1 7 11 /1 9/ i 8 18/09/ i 8 )// 1 5/ / 8 M/ ! 9/ M
oao
M
b* N)
DEER PARK PLAoTICo VCM TnA EXPOSURE
JOB
3-4 DRYING 3-4 DRYING 3-4 DRYING 3-4 DRYING 3-4 DRYING 3-4 DR* 1 NG
NAME
R. MURPHY J. NARVAEZ D. hILL I AMS T. CASKEY J. VALENZUELA J. NARVAEZ
TIME
320 320 320 320 320 32 U
DESCRIPTION
NORMAL OPER. SAMPLE VCM SAMPLING & DRY. WASHED GOWN OPER. urYER CAICH SAMPLE
VCM
O.oO 0.02 0. J3 0.28 0. 99 0. 26