Document MbobvBn1ZqrXLZJyG191Oovy

PLAINTIFF'S EXHIBIT ;:\^x -vc5 i a o \C vO I -; . ::M lam 008522 CC/G TURNAROUND INFORMATION POLICIES & PRACTICES MANUAL AUGUST 1987 DPMC-0199 LAM 008523 GENERAL INFO DPMC-01996 lam 008524 SAFETY AND ENVIRONMENTAL IMPACT STATEMENT CC&G TURNAROUND The CC&G Turnaround scheduled for September 1987 will be a larger than normal maintenance turnaround due to the fact of all the wet H2S equipment testing that has to be conducted. There will be some capital work going on during this turnaround. This work should not have any significant impact due to amount of capital work. It is imperative that we conduct this turnaround safely and within our environmental standards. The following statements address both safety and environmental standards and should be adhered to closely. SAFETY Please keep safety foremost in mind through the turnaround. Foremen and operators should not only conduct safe operations, but be alert to prevent unsafe conditions or acts in which craftsmen are involved. This includes craftsmen and craft foremen. TAGGING PROCEDURE The blind lists and procedures have been updated for each of the CC&G units. The blind lists should be followed closely. Refer to GO-121 blinding procedures. Blind tags that will be used for entry will be of two colors, orange and blue. These tags will be used at the Cat Cracker, Gas Fractionator and Gas Treaters for entry permits. Under no circumstances is a blind with an orange blue tag be pulled until entry permit has been withdrawn. All jobs will be permitted, joint jobsite inspection by Operations and Maintenance is required before a permit will be issued. Prior to the turnaround Operations should refer to S-119 on entering vessels. The permitting procedures have been changed since the last major turnaround. They must be followed. Please refer to Safety Orders S-102 (Fire and Safety Permits) and S-I03 (Department Safe Work Permits) on how to write a proper permit. Even though the units are down, the responsibility for the units and the work being performed rest with Operations. Remember nitrogen can be fatal by displacing the oxygen required for survival. Since we have many nitrogen connections in the units, before entry permits can be written plot edge blind will have to be installed at the Cat Cracker, Gas Fractionator and Gas Treaters. While catalyst is being unloaded and the regenerator, reactor and third stage cleaned internally, the entire Cat Cracker area will be a goggle and possible dust mask area. ALL personnel must wear goggles and dust masks, if necessary. We want to eliminate catalyst from getting into people's eyes. CC&G/8717003 DPMC-01997 008525 2 There is much concern about benzene being present in the equipment as the vessels and exchangers are being opened up. It has been written into out procedures to determine if benzene is present. The minimum requirement of personnel protection will be the use of an organic vapor respirator. Industrial Hygiene will be notified to test various streams in the systems at the Cat Cracker, Gas Fractionator and Gas Treaters if a portable GLC is not available. When it is necessary to drain any material into a lugger pan or garbage can a organic respirator will be required, this includes operators, craftsmen and vacuum truck drivers. These areas will be barricaded off while draining equipment. SPECIAL NOTE: The minimum DPMC respiratory requirements for benzene are outlined below: Benzene Air Concentration* Respirator Selection 1-10 ppm Half-facepiece air purifying respirator with black organic vapor cartridges 50 ppm Full-facepiece air purifying respirator with black organic vapor cartridges 1000 ppm Supplied air respirator with full-facepiece in positive pressure mode >1000 ppm Self-contained breathing apparatus with full-facepiece in positive pressure mode or full-facepiece positive pressure supplied air respirator with auxiliary self-contained air supply. *Air concentration as measured for any period of time. ENVIRONMENTAL STANDARDS In shutting down, we want to remain within our Environmental Standards and minimize the potential for environmental exceedance. After feed is cut out of the Cat Cracker, large amounts of nitrogen will be used for pressure balance and purge of the unit until the 56" blind on the outlet of the reactor is turned. Nitrogen rate on the order of 500M to 1MM SCFD will be used for a period of 8 to 12 hours after feed outage. CIB08709706 DPMC-01998 LAM 008526 3 Hydrocarbon Compressors will be shutdown and low pressure cylinders and lines will be purged to the 14" Cat Cracker relief flare via PIC-11603C. High pressure cylinders and lines will be purged via the 14" low pressure vapor relief line to the East property flare. Continued use of the 14" compressor relief with mixtures of HC vapor, steam and nitrogen purge will be necessary until water washing of main fractionator is complete and ready for isolation blinding. All blinds in the catalyst unloading system should be checked along with block valves to be sure a major catalyst spill is not experienced. Also catalyst unloading must be controlled to prevent excess catalyst from blowing out of the cyclone on top of the spent hopper. Adjust carrying air rates as necessary when this occurs. All pumps, exchangers, and fan coolers are provided with piping to purge all H.C. with nitrogen to the maintenance dropout (MDO) for recovery in V-705 flare KO pot Ph#6283 and then to V-546 Ph#6309 in West property flare system. Every effort should be made to eliminate or minimize opening bleeders to sewers while purging out these systems. However, at the Cat Cracker every effort will be made to transfer as much H.C. material back to the main fractionator and then transfer the material from the main fractionator to CC feed storage. Also vacuum trucks will be on standby to cover any problems that may come up with the MDO system. Further to minimize the risk of exceedances, no oil should be allowed to reach the storm system. We will plug storm boxes, aspirate to CCLP and vacuum trapped water to protect outfall 003. The Main Fractionator will be opened and water washed and chemically cleaned for inspection and repairs. After oil has been pumped and system drained of H.C. to Cat Cracker feed tanks water wash will begin and all wash water will be collected from slurry suction line into accumulator V-845 and then pumped to A-301 in West property Phone # 6093 for later processing through the sour water stripper system. In this manner, sulfides to the process sewer should not be a problem. All sour water from Main Fractionator into overhead products accumulator should be pumped directly into the sour water stripper. Be on the alert for unnecessary emissions. The C.O. heater opacity should not exceed 30% for more than 5 minutes in a one hour period. The TACB will allow us to exceed this limit during startup and shutdown but only if we take all reasonable steps to minimize emissions. We should operate at maximum regenerator pressure possible and the minimum superficial velocity to minimize catalyst emissions through the stack. The fourth stage catalyst recovery will continue to operate during the catalyst unloading process. CIB08709706 DPMC-01999 LAM 008527 4 Any Environmental violations to the air, water, opacity or spills must be reported to the Environmental Supervisor Phone #7212. More detail concerning the Gas Fractionator and Gas Treaters follows. ENVIRONMENTAL IMPACT GAS FRACTIONATOR In order for the turnaround to be safe and to protect the Environment each operator and foreman must carefully review each decision as to the impact on the environment. We do not want to put any oily water to the storm sewer and limit, as much as possible, the amount of oil to the process sewer. In either case, if oily/water is put to either sewer, the environmental supervisor must be notified at ext. 7217. The disposition of each sewer is as follows: PROCESS SEWER: STORM SEWER: Drains to the CCLP. (Catalytic Cracker-Lube Plant Sewer) Drains to Outfall #003, which is controlled by the CR-3 gauger (ext. 6667) The remaining oil left in the fractionator unit will be pressured out through the MDO system to V-705. Then the unit vessels, exchangers and associated piping will be cleaned by steaming. The steam condensate and oil will be routed to V-705, via the MDO system. From V-705, the oil will be pumped to V-546 and the water will be pumped to the sour water stripper. The Aromatics Department must be notified when the MDO system is utilized, as they are responsible for the flare K.O. tanks, which the MDO system is tied into. Their extension is 6283. It must be certain that the proper line-up is made when using the MDO system. Never put hot oil to the MDO line, as the tanks contain water. During the water washing step of the shutdown procedures, the water will be routed to the SWS through the MDO line. A temporary 2" line will-be installed from the MDO line to the SWS line at the East plot landing of the Fractionator. The MDO line must be blocked and the sour water line opened to route the water to the SWS. The SWS operator must be notified when the line-up is made at ext. 6238. The key contaminant of the water at the Fractionator is sulfides. If the water contains less than 40 PPM sulfides it can be put to the process sewer. The environmental supervisor must be notified prior to the release, ext. 7212. After the columns are clean, they will be purged to the East property flare with nitrogen at a rate such that there will be no flaring. CR-3 gauger must be notified when utilizing the flare system, at ext. 6667. The sulfur load to Gerbitols from the Fractionator unit will be reduced by 12-14mm scfd. To the Fuel Gas Treater the load will be reduced by l-3mm scfd. Both streams are from the Fractionator Dry Gas K.O. Pot V-1429. CC&G/8717003 DPMC-02000 LAM 008528 5 ENVIRONMENTAL IMPACT GAS TREATERS The columns at the treaters will be cleaned by steaming and water washing. At the C-3 treater the two main materials are (C-3) propane, and DEA. The DEA will be displaced to S-402, DEA storage tank. The wash water will remove trace amounts of sulfides and DEA to S-350. A DEA sample will be drawn, and a test run to determine the amount of DEA in the sample. If no DEA is found, it will be determined the water is clean and can thus be put to the process sewer. Environmental supervisor must be notified prior to release, at ext. 7212. The C-4 and C-5 treaters contain butane (C4), and pentane (C5), plus caustic. The caustic will be displaced to S-352 (spent caustic tank). The wash water will remove trace amounts of sulfides and also be stored in S-350. After the Ph is 7 and 40 PPM or less sulfides, the water will be released to the process sewer. Again the Environmental supervisor must be notified prior to the release, at ext. 7212. After the columns are clean, they will be purged to the East property flare with N2 at a rate such that there will be no flaring. If liquid containment problems occur, V-845 oily water collection vessel at Cat Cracker can be used by the Gas Fractionator for a backup via a vacuum truck. Let's all increase our awareness and our efforts to ensure this turnaround is safe and environmentally sound! The sulfur load to the Gerbitol unit from the Gas Treaters will be reduced by l-3mm scfd. This stream is from the Caustic Regenerator Columns Tops V-1413. Phone List: ACU Gauger (MDO) V-546 (MDO) ENVR. SUPERVISOR OUTFALL 003 X6283 X6309 X7212 X6667 J. W. Heidrick CIB08709706 K. 0. Lee DPMC-02001 008529 BENZENE SWEET ODOR DETECTED AT 1- 10 PPM. IRRITATES AT 100+ PEL 10 PPM KEYWORDS IMMEDIATE AND LONGTERM HEALTH HAZARD -CANCER AGENT- LEUKEMIA- CNS EFFECTS TOXICITY REPEATED EXCESSIVE EXPOSURE CAN EFFECT BLOOD SYSTEMS. ASSOC. WITH CANCER OF THE BLOOD OR LEUKEMIA. VAPOR CAN CAUSE HEADACHE, NAUSEA,ETC. SOLVENT CAN BE ABSORBED THRU SKIN AND/OR CAUSE DERMATITIS. EMBRYO FETUS TOXICITY REPORTED. PROTECTION BLACK OV MASK REQUIRED IF LIQUID PRES. ABOVE 50 PPM MUST USE AIRLINE. BLACK PVC GLOVES REQUIRED TO PREVENT SKIN DISORDERS OR ABSORPTION. REPORT TO MEDICAL IF SIGNIFICANT EXPOSURE OCCURS. CAT CRACKER GAS OIL DARK YELLOW LIQUID PEL .2 MG/M3 KEYWORDS IMMEDIATE AND LONGTERM HEALTH HAZARD -POLYCYCLIC AROMATICS-COMBUSTIBLE-- TOXICITY EXCESSIVE VAPOR EXPOSURE CAN CAUSE RESPIRATORY IRRITATION, DIZZINESS AND VOMITING. CONTACT RESULTS IN DERMATITIS. CONTAINS POLYCYCLIC AROMATICS (PCA'S) WHICH ARE ASSOCIATED WITH SKIN CANCER. MAY ALSO CAUSE OTHER SKIN DISORDERS. PROTECTION FULL FACE MASK WITH ORGANIC VAPOR BLACKCARTRIDGES AND MIST PAD OR AIRLINE RESPIRATOR REQUIRED FOR ANY OBVIOUS INHALATION HAZARD. USE HI GLO SUIT IF REQUIRED TO PREVENT SKIN CONTACT. CAT CRACKER SLURRY OIL BLACK OIL CONTAINING LOW LEVEL H2S. PEL - .2 MG/M3 KEYWORDS POLYCYCLIC AROMATICS--COMBUSTIBLE- TOXICITY INHALATION OF EXCESSIVE VAPORS CAN CAUSE RESPIRATORY IRRITATION, DIZZINESS AND VOMITING. CONTACT WITH SKIN CAN RESULT IN DERMATITIS AND OTHER SKIN DISORDERS. PCA'S IN OIL ARE ASSOCIATED WITH SKIN CANCER. H2S MAY ACCUMULATE IN TANKS. PROTECTION FULL FACE MASK WITH BLACK OV CARTRIDGESAND MIST PAD REQUIRED FOR VAPORS. IF HIGH VAPOR CONC. USE AIRLINE MASK. DUE TO PCAS AVOID ALL SKIN CONTACT. CAUSTIC SODA WATER WHITE, VIXCOUS LIQ- UID, FLAKES, OR POWDER PEL= 2 MG/CU M KEYWORDS IMMEDIATE HEALTH HAZARD IRRITANT TOXICITY SEVERE CORROSIVE ACTION ON BODY TISSUES. LONG TERM EFFECTS MAY BE DUE TO THE INHALATION OF NaOH VAPORS. PROTECTION AVOID CONTACT WITH ALL BODY TISSUES. USE LARGE AMOUNTS OF WATER TO WASH FROM BODY. DIETHANOLAMINE IDEA) WATER-WHITE LIQUID CHARACTERISITC ODOR 3 PPM TLV IMMEDIATE HEALTH HAZARD EYE AND SKIN IRRITANT TOXICITY SEVERE EYE AND SKIN IRRITANT. INHALATION OF VAPORS MAY RESULT IN IRRITATION TO NOSE, THROAT AND CHEST. PROLONGED OR REPEATED EXPOSURE MAY CAUSE LOCAL INJURY TO RESPIRATORY TRACT AND POSSIBLE LIVERAND KIDNEY DAMAGE. AVOID ALL SKIN AND EYE CONTACT. GOGGLES REQUIRED.ABOVE 3 PPM FULL-FACE RESPIRATOR WITH GREEN AM CARTRIDGES REQUIRED. CHEMICAL SUIT REQUIRED FOR TASKS ASSOCIATED WITH POTENTIAL SKIN CONTACT. ETHYL/METHYL MERCAPTAN ODOR THRESHOLD IS .25 PPB HAS DISAGREEABLE ODOR KEYWORDS PEL *= 10 PPM IMMEDIATE HEALTH HAZARD -STENCH-FLAMMABLE-NARCOTIC- TOXICITY EYE,NOSE AND THROAT IRRITANT AND NARCOTIC EFFECTS SIMILAR TO H2S AT HIGH CONC. 4PPM CAUSES HEADACHE,NAUSEA AND IRRITATION. TOXIC TO KIDNEY,AND LIVER AT HIGH CONC. FLAMMABLE. LESS TOXIC THAN H2S BUT ODOR IS LESS TOLERABLE. PROTECTION AIRLINE RESPIRATOR REQUIRED FOR ANY ANTICIPATED EXPOSURE. IF LEAK/SPILL OCCURS CONSIDER THE WORKERS DOWNWIND. DPMC-02002 *+ REFER TO THE MATERIAL SAFETY DATA SHEET FOR MORE INFORMATION ** LAM 008530 GASOLINE MIXTURE OF PETROLEUM HYDR OCARBONS PEL - 300 PPM KEYWORDS IMMEDIATE AND LONGTERM HEALTH HAZARD -FLAMMABLE------SUSPECT CARCINOGEN- TOXICITY EXCESSIVE INHALATION CAN RESULT IN IRRITATION TO RESPIRATORY TRACT AND DIZZINESS, (EX. 1000 PPM FOR 15 MIN.). SKIN CONTACT CAN RESULT IN REDNESS AND BLISTERING IF PROLONGED. KIDNEY CANCER REPORTED IN ANIMAL TESTING. PROTECTION MINIMIZE SKIN CONTACT AND INHALATION OF VAPORS. FULL FACE ORGANIC VAPOR RESPIRATOR OK UPTO 1000 PPM. HYDROGEN SULFIDE <H2S> ROTTEN EGG ODOR. DETECTOR TUBES OR SENSOR ADVISED. PEL *= 20 PPM KEYWORDS IMMEDIATE HEALTH HAZARD -IRRITATING TOXIC GAS-FLAMMABLE- TOXICITY POSSIBLY IRRITATING TO EYES AT 1 PPM} HEADACHE/DIZZINESS AT 20 PPM} AT 300 PPM UNCONCIOUSNESS IN 30-MIN. AT 500 PPM IMMEDIATE UNCONCIOUSNESS OCCURS. LOSS OF SMELL MAY OCCUR. SKIN ABSORPTION FROM GAS HAS BEEN REPORTED. PROTECTION AIR SUPPLIED RESPIRATOR REQUIRED FOR MOST EXPOSURES (SOUR TANKS, LEAKS, ETC.). DO NOT RELY ON ODOR TO DETERMINE HOW MUCH H2S THERE IS IN THE AIR. NOTE THAT GAS IS INVISIBLE. ** REFER TO THE MATERIAL SAFETY DATA SHEET FOR MORE INFORMATION ** i DPMC-02003 LAM 008531 GOGGLE AREAS SIGNS WILL BE POSTED AT UNIT ACCESSES, TOOL ROOMS, ETC.. WORK IN THE R&R AND AROUND CATALYST WILL HAVE VACUUM STATIONS FOR CRAFTSMEN TO CLEAN THEIR CLOTHES, ALONG WITH WASH BASINS FOR CLEANUP PRIOR TO LEAVING THE AREA. CRAFTSMEN WILL BE INSTRUCTED ON GOGGLE REMOVAL TO REDUCE DUST MIGRATION TO THE EYES. REFRACTORY WORK WILL REQUIRE THE USE OF FACE SHEILDS AND MONO GOGGLES (CHIPPING REFRACTORY). THE WHOLE CAT CRACKER WILL BE A GOGGLE AREA UNTIL CATALYST UNLOADING IS COMPLETE. ENTRY OF ALL CATALYST EQUIPMENT IN R&R AREA WILL REQUIRE USE OF GOGGLES. GAS TREATERS CAUSTIC AND DEA AREA - GOGGLES REQUIRED UNTIL UNIT DECONTAMINATION IS COMPLETE. OPERATIONS COORDINATOR TO DETERMINE THE TIME TO REMOVE THE REQUIREMENT. FRACTIONATOR CHEMICAL CLEANING - GOGGLES REQUIRED WHILE CHEMICAL WASHING AND SLICKER SUITS REQUIRED FOR VENTING AFTER CHEMICAL WASH. SLICKER ALSO REQUIRED WHILE WORKING ON SUCTION LINES (DRAINING THEM TO PANS) DPMC-02004 LAM 008532 HEAD KNOCKERS DURING THE SHUTDOWN THERE WILL BE AN UNUSUALLY LARGE AMOUNT OF SCAFFOLD ON THE UNIT. PLEASE MAKE EVERY EFFORT TO HIGHLIGHT THESE SCAFFOLD AREAS WITH BARRICADE FLAGS TO HELP PREVENT A POTENTIAL NECK INJURY. TRIPPING HAZARDS MAINTENANCE WILL PROVIDE RAMPS FOR TEMPORARY PIPING. WELDING LEADS AND AIR HOSES ENTERING THE REGENERATOR MANWAYS WILL BE SUSPENDED TO AID ACCESS. ANY EQUIPMENT NOT IN USE SHALL BE REMOVED TO A SAFE AREA. LOOSE ITEMS, SUCH AS NUTS AND BOLTS, WILL BE CONTAINED IN BUCKETS OR PLASTIC BINS. HOSES, NOT IN USE, SHALL BE KEPT ROLLED UP AND OUT OF NORMAL TRAFFIC AREAS. X-RAY REQUIREMENTS IN ADDITION TO BARRICADE TAPE, MAINTENANCE WILL PROVIDE FLASHING LIGHTS, AS IN THE PAST, TO WARN PERSONEL OF X-RAY IN AREA. DPMC-02005 LAM 008533 PRE-SHUT DOWN AUDIT PROJECT TITLE AUDITED BY CHECK ONLY IF AUDITED ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ ________ Planning and Information Meetings Already in Place Pre-Shut Down Safety Meetings for Operations and Crafts Establish Shut Down Audit Team .Crafts Trained on Any Toxic Chemical They May be Exposed To Emergency Evacuation Alarm Ready If Needed Staging Area and Back Up Area Selected Responsible Person to Make Head Count Scaffolding, Ladders, Platforms, Aisles and Walkv/ays Entry and Egress to Scaffolds Handrail-Toe Boards, Etc. Condition Ladder Tied Off Ladder at Proper Angle Obstructions and Tripping Hazards Valve Wrenches Available Departmental Work Permit Planned for Shut Down Operators Trained on Proper Respirator Selection for Permits Adequate Supply of Electrical Lockout Material Adequate Supply of P.P.E. - Mono Goggles, Ear Plugs, Chemical Suits, Respirators, Etc. Scott Air Paks Ready if Needed Fire Extinguishers, Hose Reels in Place if Needed Unit Checked for Adequate Lighting at Night Master Blind List on Unit Identify any Asbestos Work Area Selected for Pre-Fab Work Breathing Air Header Purged- if Necessary and Ready for Service Adequate Supply of Breathing Air on Hand Are Shower Facilities Available When Needed BDBD8602703 DPMC-02006 LAM 008534 AUDITED BY SHUTDOWN AUDIT CC&G DATE: CHECK ONLY IF AUDITED PERMITTING DEPARTMENTAL ___ _ .________ 1. 2 3. 4. JOB SITE INSPECTION MADE COMPLIANCE AUDIT OF DEPARTMENTAL WORK PERMIT HAZCOM INCLUDED ON PERMIT COMPLETE JOB DESCRIPTION FIRE AND SAFETY PERMITS _________ 1. PRE-JOB PREPARATION _________ 2. SHIFT FOREMAN INVOLVEMENT _________ 3. SOUND, SAFE WORK PROCEDURES SET OUT ON PERMIT HOUSEKEEPING _________ A. B. C. D. E. BOLTS, NUTS, ETC. ON SCAFFOLDS AND PLATFORMS HOSES, EXTENSION CORDS, WELDING LEADS NOT IN USE ARE PICKED UP OUT OF THE WAY. WALKWAYS CLEAR REMOVE BARRICADE TAPE WHEN NO LONGER NEEDED TRASH RECEPTACLES RELATIVELY EMPTY 3. WORK PRACTICES ___________ A. 12-VOLT LIGHTING IN VESSELS ___________ B. ELECTRICAL LOCKOUT PROCEDURE ___________ C. DECONTAMINATION OF LINES AND EQUIPMENT ___________ D. DEPRESSURING OF LINES AND EQUIPMENT _________ E. BARRICADING PRACTICES--OVERHEAD, CHEMICAL HAZARDS, ETC. 4. MANAGEMENT COMMITMENT _________ A. DAILY SAFETY AND PLANNING MEETINGS B. DAILY AUDITS C. TIMELY INCIDENT AND INVESTIGATION REPORTS 5. PERSONAL PROTECTIVE EQUIPMENT A. USED BY OPERATORS, CRAFTSMEN B. PROPER USE C. RETURN BREATHING AIR AND RESPIRATORS WHEN FINISHED CCG/8715403 DPMC-02007 LAM 008535 EVACUATION The Cat Cracker/Gas units are equipped with an evacuation horn. It is tested every Wednesday morning at 10:00 a.m. Should the alarm be sounded, all non-operating personnel should leave the unit immediately. Even though the unit is down, it may be necessary to evacuate, the biggest concern would be a vapor release from an adjacent unit. When the alarm sounds, calmly leave the unit - do not run. Check the wind and move in a perpendicular direction of it's path. Usually the safest place at the Cat Cracker is on the east side of the Cat Cracker. At the Gas Fract, either the northwest or northeast corner of the unit. At the Gas Treaters, go to the duplication building across the railroad tracks. Do not return to the unit!!! Operating foremen will investigate the problem. When the foremen and operators feel it is safe to return to work, the operations foremen will contact the Brown & Root Safety Man. Nobody but the operations foremen can release the crafts to resume working. All departmental work permits, unless specified by the operations foremen, will be valid. The operations foremen must have the consent of the safety man before allowing hot and entry permits to resume. CCG/8717001 DPMC-02008 LAM 008536 OJ L FINANCIAL EVACUAT\ON ^ ASS EtAfcLY P AftEA CO fAAP ,, |^8T CC$G>' SHUTD0V5W N ST S innn <R tr3l -? R/MCA _______ REFY LAB - f! 5A 1 E -1 --- - n5 tn CJ u "Ft" ST,. CCJ ENERGY RECOVER: co IBL^XJ -- ~mn m {loFJ- sgp-i JL_ PARKING' cr? CC GAS UNIl PXU CC GAS TRj R . - f- t 4 c O P d in NflRMALParaffin J. fUHT/ jtzJ M -o: SJe EVACUATION AREA PER PREVAILING WIND DIRECTION # 1 WEST OF CCU NORTH EASTERLY WINU # 2 EAST OF CCU SOUTH EASTERLY WIND # S' WEST OF GAS TREATERS SOUTH EASTERLY WIND 8 4 NORTH EAST OF GAS FRAC. NORTH EASTERLY WIND DPMC-02009 LAM 008537