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SU0004391
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SU0004391
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Last modified
12/26/2019 3:43:12 PM
Creation date
12/26/2019 3:24:07 PM
Metadata
Fields
Template:
EHD - Public
ProgramCode
2600 - Land Use Program
RECORD_ID
SU0004391
PE
2632
FACILITY_NAME
SA-01-86
STREET_NUMBER
14629
Direction
E
STREET_NAME
WILDWOOD
STREET_TYPE
RD
City
STOCKTON
ENTERED_DATE
5/19/2004 12:00:00 AM
SITE_LOCATION
14629 E WILDWOOD RD
RECEIVED_DATE
12/4/2001 12:00:00 AM
QC Status
Approved
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SJGOV\gmartinez
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EHD - Public
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Wildwood LNG Demonstration Facility <br /> 5.3 Liquefaction System <br /> The liquefaction system is the heart of the CFS technology. The proprietary cryogenic <br /> methodology that will be used for separating the nitrogen from the methane is still under <br /> development and will be tested in the proposed plant. Table 4 presents the design information <br /> used for the development of this system. <br /> The liquefaction system consists of a series of heat exchangers and separation vessels within a <br /> vacuum cold box. The purpose of the liquefaction system is to liquefy the (gaseous) natural gas <br /> to liquid natural gas through several steps of cooling and separation. This is strictly a physical <br /> process, and no chemicals or reactants are used. The two streams from the liquefaction process <br /> are the product LNG and vent gas produced during the separation steps. <br /> The vent gas generated during the separation process consists of approximately 45% nitrogen <br /> and 55% methane. The flow rate is approximately 100 scfin. The vent gas is used to regenerate <br /> the adsorbate beds in the TSA system. After regenerating the TSA beds, the gas is consumed as <br /> fuel in the engine-generator set. <br /> A closed loop refrigeration system provides the primarycooling,during the liquefaction process. <br /> After the natural gas is cooled to a liquid, it is further purified using separation vessels. After <br /> separation,the LNG product is transferred to the LNG storage tank by the system pressure. LNG <br /> product is produced at a rate of approximately four gallons per minute (gpm) at 20 psig. <br /> The proprietary elements of the CFS liquefaction system reduce the overall energy requirements <br /> by recovering a majority of the heat from the process and refrigeration streams. The streams are <br /> routed through a series of heat exchangers to either pre-cool or pre-heat the streams. This heat <br /> recovery system increases the operating efficiency and reduces the energy requirements of the <br /> system. <br /> The products from this system are the LNG product stream and the vent gas, which is used to <br /> regenerate the TSA beds and as a fuel supply for the engine-generator set. Vent gas is produced <br /> at a rate of about 100 scfm. No waste streams are produced from this system. In the event of an <br /> emergency, pressure relief valves designed to protect the vessels and piping from over <br /> pressurization may vent small quantities of natural gas into the atmosphere. <br /> Table 4 <br /> Design Information for the Liquefaction System <br /> Equipment,' Equipment Marne Pressure.(PSIG). Temperature (°F) Flow Rate <br /> Number Operatrng/Design Operating/Designscfm <br /> 40-3202 Process Gas Feed 350/400 20/100 i 600 <br /> Cooler <br /> AES Construction Group <br /> Page 7 <br />
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