초록 ▼

A system for liquefying and subcooling natural gas wherein compression power is shifted off the closed cycle refrigerant by subcooling the liquid natural gas to a relatively warm exit temperature and subsequently reducing the pressure and flashing the liquefied natural gas to recover a gaseous phase

A system for liquefying and subcooling natural gas wherein compression power is shifted off the closed cycle refrigerant by subcooling the liquid natural gas to a relatively warm exit temperature and subsequently reducing the pressure and flashing the liquefied natural gas to recover a gaseous phase natural gas in excess of plant fuel requirements, the excess being recompressed and recycled to the feed to the process.

대표청구항 ▼

1. In a process for the production of liquefied natural gas wherein a feed natural gas is liquefied and subcooled by heat exchange against at least one closed cycle refrigerant, the improvement comprising overcoming the problems of mismatched compressor drivers, inefficient liquefaction operation or

1. In a process for the production of liquefied natural gas wherein a feed natural gas is liquefied and subcooled by heat exchange against at least one closed cycle refrigerant, the improvement comprising overcoming the problems of mismatched compressor drivers, inefficient liquefaction operation or high equipment capital costs by subcooling the liquefied natural gas to a relatively warm temperature, reducing the pressure of the subcooled liquefied natural gas and flashing the same in a phase separation in at least one stage wherein a gaseous phase natural gas stream is recovered in excess of that necessary for plant fuel and the excess gaseous phase natural gas is recompressed and recycled to the feed natural gas upstream of the liquefaction and subcooling in order to shift compression power requirements from the closed cycle refrigerant to the compression requirements of the gaseous phase natural gas recycle stream. 2. The process of claim 1 wherein the closed cycle refrigerant comprises a mixture of several refrigerant components. 3. The process of claim 1 wherein the closed cycle refrigerant comprises a first closed cycle refrigerant having a single refrigerant component which precools the feed natural gas and a second closed cycle refrigerant having multiple refrigerant components which liquefies and subcools the precooled gas. 4. The process of claim 1 wherein the closed cycle refrigerant comprises a first closed cycle refrigerant having a mixture of refrigerant components which precools a second closed cycle refrigerant comprising a mixture of refrigerant components which liquefies and subcools the natural gas. 5. The process of claim 1 wherein vapors from liquefied natural gas in storage downstream of the last stage of flashing are recompressed and recycled to the gaseous phase natural gas stream. 6. The process of claim 1 wherein the gaseous phase natural gas stream is recompressed in stages with aftercooling against external cooling fluid before being reintroduced into the feed natural gas stream. 7. In a system for the production of liquefied natural gas wherein a feed natural gas stream is liquefied and subcooled against at least one closed cycle refrigerant in a multiple bundle heat exchanger, the improvement comprising means for overcoming the problems of mismatched compressor drivers, inefficient liquefaction operation or high equipment capital costs including: (a) means for reducing the pressure of the liquefied and subcooled natural gas including at least one phase separation vessel for removing a gaseous phase natural gas recycle stream; (b) compression means for recompressing the gaseous phase natural gas from said separation vessel; (c) means for removing a portion of the recompressed natural gas as plant fuel; and (d) means for introducing the remaining recompressed natural gas into the feed natural gas stream. 8. The system of claim 7 wherein the multiple bundle heat exchanger has two bundles. 9. The system of claim 7 including a precool closed cycle refrigerant stage connected to both the natural gas stream and the subcooling closed cycle refrigerant by heat exchangers. 10. The system of claim 7 including means for recycling vapors from liquefied natural gas storage to the recompression and recycle apparatus of the gaseous phase natural gas stream. 11. The system of claim 7 wherein the means of paragraph (a) includes two separate pressure reduction means and phase separation vessels. 12. The system of claim 7 including a heat exchanger for rewarming the recycled gaseous phase natural gas against process streams. 13. The system of claim 7 including conduit means for recycling the gaseous phase natural gas recycle stream from said phase separation vessel to the feed natural gas stream.