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Process for liquefying natural gas

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专利汇可以提供Process for liquefying natural gas专利检索,专利查询,专利分析的服务。并且1,011,453. Gas liquefaction process. CONCH INTERNATIONAL METHANE Ltd. July 10, 1964 [Jan. 23, 1964], No. 3017/64. Heading F4P. A process for the production of natural gas at a pressure below well head pressure and for the production of liquefied gas at a still lower pressure comprises isentropically expanding at a turbine 44 a first portion 8 of well head gas, passing the so cooled gas in indirect heat exchange at 17 with a second portion 9 of well head gas and feeding it into a distribution line 18, further cooling the said second portion of well head gas at 23, isentropically expanding it at a turbine 25, further cooling the cold expanded gas at 27 and isenthalpically expanding it at a valve 29 to produce flash gas and liquefied gas in a vessel 30 from which product liquefied gas is withdrawn by a pump 31 for storage in a vessel 33 whilst flash gas is withdrawn from vessel 30, used to cool exchangers 23, 27 after which it is compressed at 37 and passed to the distribution line 18. The first portion of well head gas is freed of methane hydrate in a separator 11 and the second portion is dried by passage through alternating molecular sieves 19, 19a which are regenerated by bleeding substantially pure methane from the compressor 37, heating at 40 and delivering it through a line 42 for use as fuel gas. The carbon dioxide content of the well head gas collects as a slurry in flash vessel 30 and is removed from the liquefied product by a centrifugal separator 32. In a modification, gas leaving turbine 25 is freed of nitrogen by absorption.,下面是Process for liquefying natural gas专利的具体信息内容。

1. A PROCESS FOR PRODUCING FROM NATURAL GAS AT HIGH PRESSURE A SUPPLY OF LIQUEFIED NATURAL GAS AT A LOWER PRESSURE THAN THE HIGH PRESSURE AT WHICH THE NATURAL GAS IS AVAILABLE WHILE DELIVERING A SECOND SUPPLY OF NATURAL GAS INTO A DISTRIBUTION PIPELINE AT AN INTERMEDIATE PRESSURE WHICH COMPRISES (A) ISENTROPICALLY EXPANDING A FIRST STREAM OF THE NATURAL GAS FROM THE HIGH PRESSURE AT WHICH IT IS AVAILABLE TO THE INTERMEDIATE PRESSURE AND SO COOLING IT, (B) PASSING THE EXPANDED AND COOLED FIRST STREAM IN INDIRECT HEAT EXCHANGED WITH A SECOND STREAM OF THE HIGH PRESSURE NATURAL GAS AND THEN INTO THE DISTRIBUTION PIPELINE, (C) FURTHER COOLING THE SECOND STREAM, (D) ISENTROPICALLY EXPANDING THE SECOND STREAM FROM STEP (C) TO COOL IT FURTHER, (E) FURTHER COOLING THE SECOND STREAM FROM STEP (D), (F) ISENTHALPICALLY EXPANDING THE SECOND STREAM FROM STEP (E) TO PRODUCE LIQUEFIED NATURAL GAS AND FLASH GAS, AND (G) PASSING THE FLASH GAS FIRSTLY TO STEP (E) AND THEN TO STEP (C) TO EFFECT THE COOLING IN THOSE STEPS AND FINALLY COMPRESSING IT TO THE INTERMEDIATE PRESSURE AND PASSING IT INTO THE DISTIBUTION PIPELINE.
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