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|LDEQ Accident Number
|Point Source(s)||Notes||Amount of Release|
|WOGF, GO-1 EF||Cause: On December 6, 2012, Shell Chemical's GO-1 flared at the GO-1 Elevated Flare (EPN 1-90). The flaring was a result of an unexpected loss of power due to the trip of an Entergy breaker supplying the GO-1 unit. The GO-1 Unit trip caused a release to the atmosphere from the GO-1 Propylene Splitter Column.|
Notes: GO-1 operations took the necessary steps to minimize flaring and safely return the unit to normal operating conditions and the flaring stopped. Data gathering to perform calculations and investigation are ongoing. Shell provided an amended final follow up notification on June 27, 2013. Reportable quantities for VOCs were exceeded. On December 9, 2012 the reportable quantities for Carbon Monoxide, Nitrogen Oxide, Particulate Matter, and 1,3-Butadiene were exceeded. On December 8, 2012 reportable quantities for particulate matter were exceeded. On a report dated June 27, 2013, the emissions of propylene and propane were amended.
|GO-1 Pressure Relief Device|
West Ops Ground Flare (EPN 9-84); GO-1 Elevated Flare (EPN 1-90)
|Cause: On June 23, 2012 Shell Chemical's GO-1 flared at the GO-1 Elevated Flare. The flaring was a result of an upset when the Propylene Refrigerant Compressor kickbacks started swinging and affecting the rest of the process unit. The swings became uncontrollable and the cold-side of GO-1 was shutdown to get the propylene refrigerant compressor and the ethylene refrigerant compressor under control. GO-1 flared process gas off the Process Gas Compressor 4th stage discharge and light fractionation columns, dry gas off the dry gas compressor discharge, and propylene and ethylene off the refrigeration compressors.
On June 23, 2012 Shell Chemical's GO-1 experienced a unit upset which led to flaring at Motiva's West Operations Ground Flare (EPN 9-84). The flaring was a result of a unit upset that caused a cold-side shutdown of the GO-1 Process Unit.|
Notes: The report was submitted more than seven days after the incident and verbal notification. GO-1 operations took the necessary steps to minimize flaring and safely return the unit to normal operating conditions and the flaring stopped. During this incident a pressure device opened to lower process pressure, releasing ethylene to the atmosphere. GO-1 operations took the necessary steps to safely return the unit to normal operating conditions and the flaring stopped. The pressure relief device closed once the pressure was lowered below the set-point. GO-1 Operations completed a Management of Change to reset the parameters in the compressor surge control system for the propylene refrigerant compressor to allow for the compressor to be restarted and prevent a reoccurrence of another similar incident. Motiva did not exceed any reportable quantities or maximum permitted limits. Shell Chemical - East exceeded its reportable quantity for highly reactive volatile organic compounds (ethylene) which was released from the a pressure relief device on GO-1 operations. It also exceeded its maximum permitted limits for 1,3 butadiene and hexane. It flared for 1 day and 21 hours (45 hours). Although Shell Chemical - East has stated that no reportable quantities were exceeded from flaring, some chemicals, such as benzene (RQ: 10 lbs) and sulfur dioxide (RQ: 500 lbs), etc. , exceeded their reportable quantities. The release of particulate matter from both flares was reported as smoking.
|Relief valve in the OL-5 Process Unit||Cause: While making an inspection round on January 12, 2012, OL-5 operators found that a relief valve in the OL-5 Process Unit was leaking out of the vent connection.
Process data does not indicate that the relief valve reached a high enough pressure to open. This relief valve has a bellows and the bellows top flange ring was found to be cracked in the rolled edge. The crack was approximately 1.5" long, and is believed to be a manufacturing defect. The valve has been returned to the manufacturer for inspection.|
Notes: The operators immediately stopped the pump that supplies the pressure to this relief valve and the relief valve was blocked in per mitigation plan. The crack was approximately 1.5" long, and is believed to be a manufacturing defect. The valve has been returned to the manufacturer for inspection. The discharged was released mainly to a stormwater concrete containment area. There is some evaporation into the atmosphere. Vacuum truck cleaned up remaining material. Only benzene was above a reportable quantity during this leak.
|GO-1 Elevated Flare (EPN 1-90)||Cause: On December 19, 2013, GO-1 had an unexpected process upset which resulted in flaring at the GO-1 Elevated Flare. The flaring was a result of a swing on the cold site of GO-1, which resulted in an upset at the propylene re-compressor.
Ending date above is the reported anticipated end date, assuming troubleshooting efforts continue as planned.|
Notes: Operations is currently stabilizing the unit and minimizing the flaring. Data gathering to perform calculations and investigation are ongoing. Shell will provide an update within 60 days.
|No information on re|
|DU-5 Unit||Cause: On September 12, 2014, Motiva's DU-5 unit received a shipment of crude oil that contained an unusually large amount of water. DU-5's normal operations removes the water from the crude and sends the water to the unit desalters. The large volume of water that was removed from the crude formed an emulsion which caused the desalter level instrumentation to malfunction. After the desalters, the water is routed to the sour water drum, but due to the instrumentation malfunction on the desalter, the water sent to the sour water drum exceeded the volume that could be pumped from the drum. The water sent to the sour water drum overflowed into the Low Pressure Flare Header. Once the water overflowed to the Low Pressure Flare Header, the liquid went to the Shell Chemical LP Utilities East Flare Pot and was combusted at the Utilities East Flare.|