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COMPLIANCE INFO_PRE 2019
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EHD Program Facility Records by Street Name
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2231-2238 – Tiered Permitting Program
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PR0546079
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COMPLIANCE INFO_PRE 2019
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Last modified
8/24/2020 10:42:19 AM
Creation date
7/30/2020 7:45:44 AM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2231-2238 – Tiered Permitting Program
File Section
COMPLIANCE INFO
FileName_PostFix
PRE 2019
RECORD_ID
PR0546079
PE
2231
FACILITY_ID
FA0003747
FACILITY_NAME
Shell Oil Products US - Stockton Terminal
STREET_NUMBER
3515
STREET_NAME
NAVY
STREET_TYPE
Dr
City
Stockton
Zip
95203
APN
161-030-02
CURRENT_STATUS
02
SITE_LOCATION
3515 Navy Dr
P_LOCATION
01
P_DISTRICT
001
QC Status
Approved
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SJGOV\gmartinez
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FilePath
\MIGRATIONS\Tiered Permitting\N\NAVY\3515\PR0546079\BILLING.PDF
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EHD - Public
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MAR-30-193 TUE 08:3,.J:SHELL STOCKTON #894 P03 <br /> E[VVn= LTD. <br /> 2.0 PROCESS DFSCRIP"17ION <br /> This section provides an overview of the GAC Fluid Bed process, from contaminated <br /> groundwater or process water feed to clean water product. A simplified description of each <br /> piece of equipment in the system is provided, as well as a discussion of the basic process theory <br /> and chemistry. <br /> 2.1 Process Overview <br /> Figure Ll presents a process flow schematic of the GAC Fluid Bed process. <br /> Influent feed enters the process through a duplex strainer to remove any large or <br /> fibrous material which may be harmful to or settle out in the plant components <br /> or piping system. Nutrients are then added to the feed. <br /> As indicated, the influent feed is mixed with part of the treated effluent recycled <br /> from the fluid bed bioreactor. The mixed stream enters the suction side of the <br /> fluidization pumps. The system hydraulics and valving are such that as the <br /> influent flow increases, the recycle flow decreases. This allows the flow through <br /> the fluidization pumps to remain essentially constant over a wide range of <br /> turndown of the influent flow. <br /> Meanwhile, oxygen is generated in a batch-type pressure-swing adsorption (PSA) <br /> system, which is supplied with dry, pressurized air from a compressor in series <br /> with a dryer. The PSA system uses a pair of pressure tanks filled with beads of <br /> zeolite which serve to hold back nitrogen molecules while allowing oxygen <br /> molecules to pass. Oxygen purity is typically 90 to 95%. The tanks are operated <br /> in an alternating mode, with one tank generating oxygen while the other is being <br /> purged of oxygen-depleted air (about 12% oxygen). An oxygen holding tank <br /> serves to smooth the delivery flow and pressure. <br /> The pressurized water leaving the fluidization pump it injected with oxygen from <br /> the PSA unit. The piping circuit includes a bubble trap, and a system for <br /> collecting, recycling, and reinjecting undissolved oxygen upstream of the bubble <br /> trap. Oxygenated water exits the bubble trap and is monitored for dissolved <br /> oxygen (and pH - optional) prior to entering the fluid bed reactor. <br /> The water stream is injected at the bottom of the fluid bed reactor vessel through <br /> an arrangement of multiple nozzles, operating in parallel via a manifold system. <br /> The nozzles assure that the water flow is distributed evenly under the fluidized <br /> bed. <br /> The fluid bed vessel contains a bed of GAC, completely immersed in water. The <br /> GAC serves two functions: 1) it provides a surface to anchor the microbes, <br /> enabling them to remain in place in a flowing water stream which would <br /> r` otherwise carry them out of the system, and 2) it adsorbs and concentrates <br /> organic molecules for the microbes to break down. <br /> Page 2-1 <br />
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