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11. 发明公开

EP1745254A2 NATURAL GAS LIQUEFACTION 审中-公开
标题翻译：天然气液化
公开(公告)号：EP1745254A2
公开(公告)日：2007-01-24
申请号：EP05741264.5
申请日：2005-04-28
申请人： Ortloff Engineers, Ltd
发明人： WILKINSON, John, D. , LYNCH, Joe, T. , HUDSON, Hank, M. , CUELLAR, Kyle, T.
IPC分类号： F25J1/00 , F25J3/00
CPC分类号： F25J1/0216 , F25J1/0022 , F25J1/0035 , F25J1/0045 , F25J1/0052 , F25J1/0057 , F25J1/0205 , F25J1/0214 , F25J1/0239 , F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J3/0247 , F25J2200/02 , F25J2200/04 , F25J2200/30 , F25J2200/70 , F25J2200/74 , F25J2200/78 , F25J2205/04 , F25J2230/08 , F25J2230/20 , F25J2230/60 , F25J2240/02 , F25J2240/30 , F25J2270/02 , F25J2270/12 , F25J2270/60 , F25J2270/66 , F25J2290/40
摘要： A process for liquefying natural gas in conjunction with producing a liquid stream containing predominantly hydrocarbons heavier than methane is disclosed. In the process, the natural gas stream to be liquefied is partially cooled and divided into first and second streams. The first stream is further cooled to condense substantially all of it, expanded to an intermediate pressure, and then supplied to a distillation column at a first mid-column feed position. The second stream is also expanded to intermediate pressure and is then supplied to the column at a second lower mid-column feed position. A distillation stream is withdrawn from the column below the feed point of the second stream and is cooled to condense at least a part of it, forming a reflux stream. At least a portion of the reflux stream is directed to the distillation column as its top feed.
摘要翻译：公开了液化天然气以及生产主要含有比甲烷重的烃的液体流的方法。在该过程中，待液化的天然气流被部分冷却并分成第一和第二物流。第一物流进一步冷却以基本上全部冷凝，膨胀至中间压力，然后在第一中间塔进料位置供应至蒸馏塔。第二物流也膨胀到中间压力，然后在第二个中间中柱进料位置供应到塔。将蒸馏物流从第二物流进料点之下的塔中排出，并将其冷却至至少一部分冷凝物，形成回流物流。至少一部分回流物流作为其顶部进料被引导至蒸馏塔。

12. 发明公开

EP3044528A1 HYDROCARBON GAS PROCESSING 审中-公开
标题翻译： BEHANDLUNG冯KOHLENWASSERSTOFFGAS
公开(公告)号：EP3044528A1
公开(公告)日：2016-07-20
申请号：EP14843550.6
申请日：2014-08-18
申请人： Ortloff Engineers, Ltd , S.M.E. Products LP
发明人： MILLER, Scott, A. , WILKINSON, John, D. , LYNCH, Joe, T. , HUDSON, Hank, M. , CUELLAR, Kyle, T. , JOHNKE, Andrew, F. , LEWIS, W., Larry
IPC分类号： F25J3/02 , F25J3/08
CPC分类号： C07C7/09 , B01D3/26 , B01D3/32 , B01D3/322 , B01D5/0063 , C10G5/06 , C10L3/06 , C10L2290/06 , C10L2290/48 , C10L2290/541 , C10L2290/543 , C10L2290/545 , F25J1/0022
摘要： A process and an apparatus are disclosed for a compact processing assembly to remove C5 and heavier hydrocarbon components from a hydrocarbon gas stream. The hydrocarbon gas stream is expanded to lower pressure and supplied to the processing assembly between an absorbing means and a mass transfer means. A distillation vapor stream is collected from the upper region of the absorbing means and cooled in a first heat and mass transfer means inside the processing assembly to partially condense it, forming a residual vapor stream and a condensed stream. The condensed stream is supplied to the absorbing means at its top feed point. A distillation liquid stream is collected from the lower region of the mass transfer means and directed into a second heat and mass transfer means inside the processing assembly to heat it and strip out its volatile components.
摘要翻译：公开了一种用于紧凑加工组件以从烃气流中除去C5和较重烃组分的方法和装置。将烃气流膨胀到较低的压力，并在吸收装置和传质装置之间提供给处理组件。蒸馏蒸气流从吸收装置的上部区域收集，并在处理组件内部的第一热传质装置中冷却，以使其部分冷凝，形成残余蒸气流和冷凝流。冷凝的流在其顶部进料点处供应到吸收装置。蒸馏液流从质量传递装置的下部区域收集并且被引导到处理组件内部的第二打浆和传质装置中，以加热它并剥离其挥发性组分。

13. 发明公开

EP2575996A1 HYDROCARBON GAS PROCESSING 审中-公开
标题翻译：碳氢气体处理
公开(公告)号：EP2575996A1
公开(公告)日：2013-04-10
申请号：EP11790241.1
申请日：2011-05-27
申请人： Ortloff Engineers, Ltd
发明人： CUELLAR, Kyle, T. , WILKINSON, John, D. , HUDSON, Hank, M.
IPC分类号： B01D19/00
CPC分类号： F25J3/0266 , F25J3/0209 , F25J3/0219 , F25J3/0223 , F25J3/0233 , F25J3/0252 , F25J2200/02 , F25J2200/70 , F25J2205/02 , F25J2205/04 , F25J2210/12 , F25J2220/82 , F25J2230/08 , F25J2230/60 , F25J2230/80 , F25J2235/80 , F25J2240/02 , F25J2245/02 , F25J2260/80 , F25J2270/02 , F25J2270/12 , Y02C10/04 , Y02C10/12
摘要： A process and an apparatus are disclosed for removing carbon dioxide from a hydrocarbon gas stream. The gas stream is cooled, expanded to intermediate pressure, and supplied to a fractionation tower at a top column feed position. The tower overhead vapor stream is compressed to higher pressure and cooled to partially condense it, forming a condensed stream. The condensed stream is expanded to intermediate pressure, used to subcool a portion of the tower bottom liquid product, then supplied to the tower at a mid-column feed position. The subcooled portion of the tower bottom liquid product is expanded to lower pressure and used to cool the compressed overhead vapor stream. The quantities and temperatures of the feeds to the fractionation tower are effective to maintain the overhead temperature of the fractionation tower at a temperature whereby the major portion of the carbon dioxide is recovered in the tower bottom liquid product.
摘要翻译：公开了一种用于从烃气流中除去二氧化碳的方法和装置。气流被冷却，膨胀到中间压力，并被供应到顶部塔进料位置的分馏塔。塔顶蒸气流被压缩到更高的压力并冷却，使其部分冷凝，形成冷凝物流。冷凝的物流膨胀到中间压力，用于过冷部分塔底液体产物，然后在中间塔进料位置供应到塔。塔底液体产品的过冷部分膨胀至较低压力并用于冷却压缩的塔顶蒸气流。进入分馏塔的进料的量和温度有效地将分馏塔的塔顶温度保持在一定温度，由此大部分二氧化碳被回收到塔底液体产物中。

14. 发明公开

EP2480846A1 HYDROCARBON GAS PROCESSING 审中-公开
标题翻译：碳氢气体处理
公开(公告)号：EP2480846A1
公开(公告)日：2012-08-01
申请号：EP10817651.2
申请日：2010-08-27
申请人： Ortloff Engineers, Ltd
发明人： MARTINEZ, Tony, L. , WILKINSON, John, D. , LYNCH, Joe, T. , HUDSON, Hank, M. , CUELLAR, Kyle, T.
IPC分类号： F25J3/00
CPC分类号： F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J2200/02 , F25J2200/30 , F25J2200/74 , F25J2200/76 , F25J2200/78 , F25J2200/90 , F25J2200/92 , F25J2200/94 , F25J2205/04 , F25J2210/06 , F25J2210/60 , F25J2215/60 , F25J2230/08 , F25J2235/60 , F25J2240/02 , F25J2240/40 , F25J2270/02 , F25J2270/12 , F25J2290/12 , F25J2290/40
摘要： A process and an apparatus are disclosed for the recovery of ethane, ethylene, propane, propylene, and heavier hydrocarbon components from a hydrocarbon gas stream The stream is cooled and divided into first and second streams The first stream is further cooled to condense substantially all of it and is thereafter expanded to the fractionation tower pressure and supplied to the fractionation tower at an upper mid-column feed position The second stream is expanded to the tower pressure and supplied to the column at a mid-column feed position A distillation vapor stream is withdrawn from the column above the feed point of the first stream, combined with a portion of the tower overhead vapor stream, compressed to higher pressure, and directed into heat exchange relation with the remaining tower overhead vapor stream to cool the compressed combined vapor stream and condense at least a part of it, forming a condensed stream
摘要翻译：公开了一种用于从烃气流中回收乙烷，乙烯，丙烷，丙烯和较重烃组分的方法和设备。该气流被冷却并分成第一和第二流。第一流进一步冷却以冷凝基本上全部的然后膨胀至分馏塔压力并在上部中间塔进料位置供应至分馏塔。第二料流膨胀至塔压并在中间塔进料位置供应至塔。蒸馏蒸气流为从第一物流进料点上方的塔中取出，与一部分塔顶蒸汽物流合并，压缩至较高压力，并与剩余塔顶馏出物蒸气物流进行热交换以冷却压缩的合并蒸气物流，并且至少冷凝其一部分，形成冷凝物流

15. 发明公开

EP2324312A1 LIQUEFIED NATURAL GAS PRODUCTION 审中-公开
标题翻译：生产液化天然气
公开(公告)号：EP2324312A1
公开(公告)日：2011-05-25
申请号：EP09805364.8
申请日：2009-07-28
申请人： Ortloff Engineers, Ltd
发明人： WILKINSON, John, D. , HUDSON, Hank, M. , CUELLAR, Kyle, T.
IPC分类号： F25J3/00
CPC分类号： F25J1/0231 , F25J1/0022 , F25J1/0035 , F25J1/0037 , F25J1/004 , F25J1/0045 , F25J1/0201 , F25J1/023 , F25J1/0232 , F25J3/0209 , F25J3/0233 , F25J2200/02 , F25J2200/72 , F25J2205/04 , F25J2210/06 , F25J2215/02 , F25J2215/04 , F25J2220/64 , F25J2230/60 , F25J2240/02 , F25J2245/02 , F25J2245/90 , F25J2260/10 , F25J2260/60 , F25J2270/02
摘要： A process and an apparatus for liquefying a portion of a natural gas stream are disclosed. The natural gas stream is cooled under pressure and divided into a first stream and a second stream. The first stream is cooled, expanded to an intermediate pressure, and supplied to a lower feed point on a distillation column. The second stream is expanded to the intermediate pressure and divided into two portions. One portion is cooled and then supplied to a mid-column feed point on the distillation column; the other portion is used to cool the first stream. The bottom product from this distillation column preferentially contains the majority of any hydrocarbons heavier than methane that would otherwise reduce the purity of the liquefied natural gas, so that the overhead vapor from the distillation column contains essentially only methane and lighter components.

16. 发明公开

EP1740897A1 NATURAL GAS LIQUEFACTION 审中-公开
标题翻译：天然气液化
公开(公告)号：EP1740897A1
公开(公告)日：2007-01-10
申请号：EP04822020.6
申请日：2004-04-26
申请人： Ortloff Engineers, Ltd
发明人： WILKINSON, John, D. , HUDSON, Hank, M. , CUELLAR, Kyle, T.
IPC分类号： F25J1/00 , F25J3/00
CPC分类号： F25J1/0214 , F25J1/0022 , F25J1/0035 , F25J1/0042 , F25J1/0045 , F25J1/0052 , F25J1/0057 , F25J1/0205 , F25J1/0216 , F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J2200/02 , F25J2200/74 , F25J2200/80 , F25J2205/04 , F25J2230/08 , F25J2230/60 , F25J2240/02 , F25J2240/30 , F25J2270/02 , F25J2270/12 , F25J2270/60 , F25J2270/66
摘要： A process for liquefying natural gas in conjunction with producing a liquid stream containing predominantly hydrocarbons heavier than methane is disclosed. In the process, the natural gas stream to be liquefied is partially cooled, expanded to an intermediate pressure, and supplied to a distillation column. The bottom product from this distillation column preferentially contains the majority of any hydrocarbons heavier than methane that would otherwise reduce the purity of the liquefied natural gas. The residual gas stream from the distillation column is compressed to a higher intermediate pressure, cooled under pressure to condense it, and then expanded to low pressure to form the liquefied natural gas stream.
摘要翻译：公开了液化天然气以及生产主要含有比甲烷重的烃的液体流的方法。在该过程中，待液化的天然气流部分冷却，膨胀至中间压力，并供应至蒸馏塔。来自该蒸馏塔的底部产物优选含有大部分比甲烷重的任何烃，否则会降低液化天然气的纯度。来自蒸馏塔的残余气流被压缩到更高的中间压力，在压力下冷却以冷凝它，然后膨胀到低压以形成液化天然气流。

17. 发明公开

EP2553368A1 HYDROCARBON GAS PROCESSING 审中-公开
标题翻译：处理烃类气体
公开(公告)号：EP2553368A1
公开(公告)日：2013-02-06
申请号：EP11763217.4
申请日：2011-03-17
申请人： Ortloff Engineers, Ltd , S.M.E. Products LP
发明人： JOHNKE, Andrew, F. , LEWIS, W. Larry , TYLER, L., Don , WILKINSON, John, D. , LYNCH, Joe, T. , HUDSON, Hank, M. , CUELLAR, Kyle, T.
IPC分类号： F25J3/02
CPC分类号： F25J3/0209 , C10G5/06 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2200/80 , F25J2205/02 , F25J2205/04 , F25J2210/06 , F25J2235/60 , F25J2240/02 , F25J2250/20 , F25J2270/02 , F25J2270/12 , F25J2270/60 , F25J2290/40 , F25J2290/42
摘要： A process and an apparatus are disclosed for a compact processing assembly to recover C
2 components (or C
3 components) and heavier hydrocarbon components from a hydrocarbon gas stream. The gas stream is cooled and divided into first and second streams. The first stream is further cooled to condense substantially all of it, expanded to lower pressure, and supplied as top feed to an absorbing means. The second stream is also expanded to lower pressure and fed to the bottom of the absorbing means. A distillation vapor stream from the absorbing means is heated by cooling the gas stream and the first stream. A distillation liquid stream from the absorbing means is fed to a heat and mass transfer means to heat it and strip out its volatile components while cooling the gas stream. The absorbing means and the heat and mass transfer means are housed in the processing assembly.

18. 发明公开

EP2553367A1 HYDROCARBON GAS PROCESSING 审中-公开
标题翻译：碳氢气体处理
公开(公告)号：EP2553367A1
公开(公告)日：2013-02-06
申请号：EP11766369.0
申请日：2011-03-18
申请人： Ortloff Engineers, Ltd , S.M.E. Products LP
发明人： JOHNKE, Andrew, F. , LEWIS, W., Larry , TYLER, L., Don , WILKINSON, John, D. , LYNCH, Joe, T. , HUDSON, Hank, M. , CUELLAR, Kyle, T.
IPC分类号： F25J3/00
CPC分类号： F25J3/0209 , C10G70/041 , C10G70/046 , F25J3/0233 , F25J3/0242 , F25J2200/02 , F25J2200/30 , F25J2200/74 , F25J2200/78 , F25J2200/80 , F25J2205/02 , F25J2205/04 , F25J2210/06 , F25J2235/60 , F25J2240/02 , F25J2250/20 , F25J2270/12 , F25J2270/60 , F25J2290/40
摘要： A process and an apparatus are disclosed for a compact processing assembly to recover propane, propylene, and heavier hydrocarbon components from a hydrocarbon gas stream. The gas stream is cooled, expanded to lower pressure, and fed to an absorbing means. A first distillation liquid stream from the absorbing means is fed to a mass transfer means. A first distillation vapor stream from the mass transfer means is cooled to partially condense it, forming a residual vapor stream and a condensed stream. The condensed stream is supplied as the top feed to the absorbing means. A second distillation vapor stream from the absorbing means is heated by cooling the first distillation vapor stream, combined with the residual vapor stream, and heated by cooling the gas stream. A second distillation liquid stream from the mass transfer means is heated in a heat and mass transfer means to strip out its volatile components.
摘要翻译：公开了一种用于紧凑处理组件以从烃气流中回收丙烷，丙烯和较重烃组分的方法和装置。气流被冷却，膨胀到较低的压力，并被输送到吸收装置。来自吸收装置的第一蒸馏液流被送入质量传递装置。来自传质装置的第一蒸馏蒸气流被冷却以使其部分冷凝，形成残留蒸气流和冷凝流。冷凝物流作为顶部进料提供给吸收装置。来自吸收装置的第二蒸馏蒸气流通过冷却第一蒸馏蒸气流，与残余蒸气流结合并通过冷却气流加热来加热。来自质量传递装置的第二蒸馏液流在传热和传质装置中被加热以去除其挥发性组分。

19. 发明公开

EP2553365A1 HYDROCARBON GAS PROCESSING 审中-公开
标题翻译：碳氢气体处理
公开(公告)号：EP2553365A1
公开(公告)日：2013-02-06
申请号：EP11763227.3
申请日：2011-03-21
申请人： Ortloff Engineers, Ltd , S.M.E. Products LP
发明人： JOHNKE, Andrew, F. , LEWIS, W., Larry , TYLER, L., Don , WILKINSON, John, D. , LYNCH, Joe, T. , HUDSON, Hank, M. , CUELLAR, Kyle, T.
IPC分类号： F25J3/00
CPC分类号： F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/78 , F25J2200/80 , F25J2205/02 , F25J2205/04 , F25J2210/06 , F25J2235/60 , F25J2240/02 , F25J2250/20 , F25J2270/12 , F25J2270/60 , F25J2290/40 , F25J2290/42
摘要： A process and an apparatus are disclosed for a compact processing assembly to recover C
2 (or C
3 ) components and heavier hydrocarbon components from a hydrocarbon gas stream. The gas stream is cooled and divided into first and second streams. The first stream is further cooled, expanded to lower pressure, and supplied as a feed between two absorbing means. The second stream is expanded to lower pressure and supplied as a bottom feed to the lower absorbing means. A distillation liquid stream from the bottom of the lower absorbing means is heated in a heat and mass transfer means to strip out its volatile components. A distillation vapor stream from the top of the heat and mass transfer means is cooled by a distillation vapor stream from the top of the upper absorbing means, thereby forming a condensed stream that is supplied as a top feed to the upper absorbing means.
摘要翻译：公开了一种用于紧凑处理组件以从烃气体流中回收C 2（或C 3）组分和较重烃组分的方法和装置。气流被冷却并分成第一和第二流。第一物流进一步冷却，膨胀至较低压力，并作为两个吸收装置之间的进料供应。第二物流膨胀至较低压力并作为底部进料供应至下部吸收装置。来自下部吸收装置底部的蒸馏液流在传热和传质装置中被加热以去除其挥发性组分。来自传热和传质装置顶部的蒸馏蒸汽流被来自上部吸收装置顶部的蒸馏蒸气流冷却，由此形成冷凝物流，该冷凝物流作为顶部进料被提供给上部吸收装置。

20. 发明公开

EP2440867A1 HYDROCARBON GAS PROCESSING 审中-公开
标题翻译：碳氢气体处理
公开(公告)号：EP2440867A1
公开(公告)日：2012-04-18
申请号：EP10786524.8
申请日：2010-03-31
申请人： Ortloff Engineers, Ltd , SME Products, LP
发明人： JOHNKE, Andrew, F. , LEWIS, W., Larry , WILKINSON, John, D. , LYNCH, Joe, T. , HUDSON, Hank, M. , CUELLAR, Kyle, T.
IPC分类号： F25J3/00
CPC分类号： C10G5/06 , C10G2400/20 , F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/30 , F25J2200/70 , F25J2200/78 , F25J2200/80 , F25J2205/04 , F25J2210/06 , F25J2210/12 , F25J2240/02 , F25J2270/12 , F25J2270/60 , F25J2290/40 , F25J2290/42 , Y02C20/20
摘要： A process and an apparatus are disclosed for the recovery of propane, propylene, and heavier hydrocarbon components from a hydrocarbon gas stream in a compact processing assembly. The gas stream is cooled, expanded to lower pressure, and supplied as the bottom feed to an absorbing means inside the processing assembly. A first distillation liquid stream is collected from the lower region of the absorbing means and supplied as the top feed to a mass transfer means inside the processing assembly. A first distillation vapor stream is collected from the upper region of the mass transfer means and cooled sufficiently to at least partially condense it, forming a residual vapor stream and a condensed stream. The condensed stream is supplied as the top feed to the absorbing means. A second distillation vapor stream is collected from the upper region of the absorbing means and directed into one or more heat exchange means inside the processing assembly to heat it while cooling the first distillation vapor stream. The heated second distillation vapor stream is combined with any of the residual vapor stream and the combined stream is directed into the one or more heat exchange means inside the processing assembly to heat it while cooling the gas stream. A second distillation liquid stream is collected from the lower region of the mass transfer means and directed into a heat and mass transfer means inside the processing assembly to heat it and strip out its volatile components. The quantities and temperatures of the feeds to the absorbing means are effective to maintain the temperature of the upper region of the absorbing means at a temperature whereby the major portions of the desired components are recovered in the stripped second distillation liquid stream.
摘要翻译：公开了一种用于在紧凑处理组件中从烃气流中回收丙烷，丙烯和较重烃组分的方法和设备。气流被冷却，膨胀到较低的压力，并作为底部进料供应到处理组件内的吸收装置。从吸收装置的下部区域收集第一蒸馏液流，并将其作为顶部进料提供给处理组件内部的传质装置。从传质装置的上部区域收集第一蒸馏蒸气流并充分冷却以至少部分冷凝它，形成残留蒸气流和冷凝流。冷凝物流作为顶部进料提供给吸收装置。从吸收装置的上部区域收集第二蒸馏蒸气流并将其导入处理组件内部的一个或多个热交换装置，以在冷却第一蒸馏蒸气流的同时加热它。将加热的第二蒸馏蒸气流与任何残余蒸气流合并，并将合并的流引入处理组件内部的一个或多个热交换装置，以在冷却气流的同时将其加热。从传质装置的下部收集第二蒸馏液流并将其引入处理组件内部的传热和传质装置中，以加热其并将其挥发性组分除去。进入吸收装置的进料的量和温度有效地将吸收装置的上部区域的温度维持在一个温度，由此大部分所需组分被回收在汽提过的第二蒸馏液流中。

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