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公开(公告)号:US09605896B2
公开(公告)日:2017-03-28
申请号:US13643261
申请日:2011-04-28
申请人: Xavier Renaud
发明人: Xavier Renaud
CPC分类号: F25J3/0266 , F25J3/0209 , F25J3/0233 , F25J3/0242 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2205/02 , F25J2205/04 , F25J2215/04 , F25J2220/84 , F25J2230/30 , F25J2230/80 , F25J2235/80 , F25J2260/80 , F25J2270/02 , F25J2270/80 , F25J2290/72 , Y02C10/12
摘要: The disclosure includes a process for treating a natural gas containing carbon dioxide wherein the natural gas is separated by a cryogenic process in order to provide, on the one hand, a stream of liquid carbon dioxide, containing hydrocarbons, and, on the other hand, purified natural gas; at least one part of the natural gas is cooled in a first heat exchanger and then in a second heat exchanger before the cryogenic process and/or before a reflux to the cryogenic process; at least one part of the stream of liquid carbon dioxide is recovered in order to provide a stream of recycled carbon dioxide; the stream of recycled carbon dioxide is divided into a first portion and a second portion; the first portion is expanded and then heated in the first heat exchanger, in order to provide a first stream of heated carbon dioxide; the second portion is cooled, then at least one part of the second portion is expanded and then heated in the second heat exchanger, in order to provide a second stream of heated carbon dioxide; at least some of the hydrocarbons contained in the first stream of heated carbon dioxide and in the second stream of heated carbon dioxide are recovered by liquid/gas separation.
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公开(公告)号:US20130036765A1
公开(公告)日:2013-02-14
申请号:US13643261
申请日:2011-04-28
申请人: Xavier Renaud
发明人: Xavier Renaud
IPC分类号: F25J3/08
CPC分类号: F25J3/0266 , F25J3/0209 , F25J3/0233 , F25J3/0242 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2205/02 , F25J2205/04 , F25J2215/04 , F25J2220/84 , F25J2230/30 , F25J2230/80 , F25J2235/80 , F25J2260/80 , F25J2270/02 , F25J2270/80 , F25J2290/72 , Y02C10/12
摘要: The disclosure includes a process for treating a natural gas containing carbon dioxide wherein the natural gas is separated by a cryogenic process in order to provide, on the one hand, a stream of liquid carbon dioxide, containing hydrocarbons, and, on the other hand, purified natural gas; at least one part of the natural gas is cooled in a first heat exchanger and then in a second heat exchanger before the cryogenic process and/or before a reflux to the cryogenic process; at least one part of the stream of liquid carbon dioxide is recovered in order to provide a stream of recycled carbon dioxide; the stream of recycled carbon dioxide is divided into a first portion and a second portion; the first portion is expanded and then heated in the first heat exchanger, in order to provide a first stream of heated carbon dioxide; the second portion is cooled, then at least one part of the second portion is expanded and then heated in the second heat exchanger, in order to provide a second stream of heated carbon dioxide; at least some of the hydrocarbons contained in the first stream of heated carbon dioxide and in the second stream of heated carbon dioxide are recovered by liquid/gas separation.
摘要翻译: 本公开包括用于处理含二氧化碳的天然气的方法,其中天然气通过低温方法分离,以便一方面提供含有烃的液态二氧化碳流,另一方面, 净化天然气; 至少一部分天然气在第一热交换器中冷却,然后在第二热交换器中在低温过程之前和/或在回流到低温过程之前冷却; 回收液态二氧化碳流的至少一部分以提供再循环二氧化碳流; 再循环二氧化碳流被分成第一部分和第二部分; 第一部分被膨胀,然后在第一热交换器中加热,以便提供第一加热二氧化碳流; 第二部分被冷却,然后将第二部分的至少一部分膨胀,然后在第二热交换器中加热,以便提供第二加热二氧化碳流; 通过液体/气体分离回收加热二氧化碳的第一流中和加热的二氧化碳的第二流中包含的至少一些烃。
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公开(公告)号:US20060239879A1
公开(公告)日:2006-10-26
申请号:US11389113
申请日:2006-03-27
IPC分类号: B01D53/46
CPC分类号: B01D53/26 , B01D53/002 , B01D53/1462 , C10L3/102 , C10L3/106 , F25J3/0209 , F25J3/0233 , F25J3/0242 , F25J3/0266 , F25J3/061 , F25J3/0635 , F25J3/0645 , F25J3/067 , F25J2200/02 , F25J2220/60 , F25J2220/66 , F25J2235/60 , F25J2240/02 , F25J2240/40 , F25J2270/12 , Y02C10/12
摘要: The method allows pretreatment of an acid gas that can comprise more than 10% H2S, for example a natural gas or a gas associated with the production of a crude petroleum effluent. The gas is dehydrated in unit DH, then cooled by heat exchangers E9 to E12 and by expansion carried out through valve V7. Cooling allows part of the H2S contained in the gas to be condensed. The condensates are separated from the gas in drum B1. The liquid recovered at the bottom of drum B1 is pumped and injected into well P to be sequestered in an underground reservoir or a geologic structure. The gas discharged at the top of drum B1 is depleted in H2S. This gas is sent through line 43 to a treating site in order to be subjected to additional treatments prior to being used.
摘要翻译: 该方法允许预处理可以包含超过10%H 2 S的酸性气体,例如与生产粗石油流出物相关的天然气或气体。 气体在单元DH中脱水,然后通过热交换器E 9至E 12冷却,并通过阀V 7进行膨胀。 冷却使得包含在气体中的部分H 2 S 3被冷凝。 将冷凝物与鼓B 1中的气体分离。将在桶B 1底部回收的液体泵入并注入井P中以将其隔离在地下储层或地质结构中。 在鼓B1的顶部排放的气体耗尽H 2 S。 该气体通过管线43送至处理部位,以便在使用之前进行额外的处理。
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