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1. 发明授权

US5983664A Hydrocarbon gas processing 失效
标题翻译：烃类气体加工
公开(公告)号：US5983664A
公开(公告)日：1999-11-16
申请号：US54802
申请日：1998-04-03
申请人： Roy E. Campbell, deceased , John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
发明人： Roy E. Campbell, deceased , John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
IPC分类号： F25J3/02 , F25J3/00
CPC分类号： F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J2200/02 , F25J2200/50 , F25J2200/70 , F25J2200/76 , F25J2205/04 , F25J2210/12 , F25J2235/60 , F25J2240/02
摘要： A process for the recovery of ethane, ethylene, propane, propylene and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed. In recent years, the preferred method of separating a hydrocarbon gas stream generally includes supplying at least a portion of the gas stream to a work expansion device, then directing the work expanded stream to a distillation column at a mid-column feed point below an upper rectification section. The top column feed above the upper rectification section is typically a condensed and subcooled gaseous stream, frequently comprised of a gas stream that would otherwise feed the work expansion device. In the process disclosed, the work expanded stream is further cooled prior to feeding the distillation column at the mid-column feed point, so that a lesser volume of top column feed is required to maintain the column overhead temperature at a temperature whereby the major portion of the desired components is recovered.
摘要翻译：公开了从烃气流中回收乙烷，乙烯，丙烷，丙烯和较重烃组分的方法。近年来，分离烃气流的优选方法通常包括将至少一部分气体流供应到工作膨胀装置，然后将工作膨胀流引导到蒸馏塔，该蒸馏塔位于上部下方的中间柱进料点整改部分。上部精馏段上方的顶部塔进料通常是冷凝的和过冷的气态物流，其通常由气流组成，否则气体将进料工作膨胀装置。在所公开的方法中，将工作膨胀的料流进一步冷却，然后在中间塔进料点进料蒸馏塔，使得需要较少量的顶部塔进料以将塔顶馏出物温度保持在一定温度，的所需组分被回收。

2. 发明授权

US5881569A Hydrocarbon gas processing 失效
标题翻译：烃类气体加工
公开(公告)号：US5881569A
公开(公告)日：1999-03-16
申请号：US915065
申请日：1997-08-20
申请人： Roy E. Campbell, deceased , John D. Wilkinson , Hank M. Hudson , Kyle T. Cueller
发明人： Roy E. Campbell, deceased , John D. Wilkinson , Hank M. Hudson , Kyle T. Cueller
IPC分类号： F25J3/02
CPC分类号： F25J3/0242 , F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J2200/02 , F25J2200/70 , F25J2200/76 , F25J2205/04 , F25J2210/06 , F25J2210/12 , F25J2230/30 , F25J2235/60 , F25J2240/02 , F25J2245/02 , F25J2270/02 , F25J2270/12 , F25J2270/60
摘要： A process for the recovery of ethane, ethylene, propane, propylene and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed. The stream is divided into first and second streams, and the second stream is expanded to the fractionation tower pressure and supplied to the column at a mid-column feed position. A recycle stream is withdrawn from the tower overhead after it has been warmed and compressed, and is combined with the first stream. The combined stream is cooled to condense substantially all of it, and is thereafter expanded to the fractionation tower pressure and supplied to the fractionation tower at a top column feed position. The pressure of the compressed recycle stream and the quantities and temperatures of the feeds to the column are effective to maintain the column overhead temperature at a temperature whereby the major portion of the desired components is recovered.
摘要翻译：公开了从烃气流中回收乙烷，乙烯，丙烷，丙烯和较重烃组分的方法。将该流分成第一和第二流，并将第二流扩展至分馏塔压力，并在中间柱进料位置供应至塔。在塔架顶部被加热和压缩之后，再循环流从第一塔流出。将合并的流冷却以基本上将其冷凝，然后将其扩展至分馏塔压力，并在顶部塔进料位置供应至分馏塔。压缩的再循环料流的压力以及进料塔的进料的数量和温度对塔顶温度的维持是有效的，从而回收主要部分的所需组分。

3. 发明授权

US09021832B2 Hydrocarbon gas processing 有权
标题翻译：烃类气体加工
公开(公告)号：US09021832B2
公开(公告)日：2015-05-05
申请号：US12979563
申请日：2010-12-28
申请人： Michael C. Pierce , John D. Wilkinson , Hank M. Hudson
发明人： Michael C. Pierce , John D. Wilkinson , Hank M. Hudson
IPC分类号： F25J3/02
CPC分类号： F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J2200/04 , F25J2200/70 , F25J2200/72 , F25J2200/74 , F25J2200/78 , F25J2200/94 , F25J2205/04 , F25J2210/12 , F25J2230/30 , F25J2235/60 , F25J2240/02 , F25J2245/02 , F25J2270/12 , F25J2270/60
摘要： A process and an apparatus are disclosed for recovering ethane, ethylene, and heavier hydrocarbon components from a hydrocarbon gas stream. The stream is cooled, expanded to lower pressure, and supplied to a first fractionation tower at a mid-column feed position. A distillation liquid stream is withdrawn from the first fractionation tower below the feed position of the expanded stream, heated, and directed into a second fractionation tower that produces an overhead vapor stream and a bottom liquid stream. The overhead vapor stream is cooled to condense it, with a portion of the condensed stream directed to the second fractionation tower as its top feed and the remainder directed to the first fractionation tower at a lower column feed position. The bottom liquid stream from the second fractionation tower is cooled and directed to the first fractionation tower as its top feed.
摘要翻译：公开了从烃气流中回收乙烷，乙烯和较重烃组分的方法和装置。将料流冷却，膨胀至较低压力，并在中间柱进料位置供应至第一分馏塔。蒸馏液体流从第一分馏塔排出到膨胀物流的进料位置以下，被加热，并引导到产生顶部蒸汽流和底部液体物流的第二分馏塔中。将塔顶蒸气物流冷却以使其冷凝，一部分冷凝物流作为其顶部进料引导至第二分馏塔，其余部分以较低塔进料位置引导至第一分馏塔。将来自第二分馏塔的底部液体物流冷却并引导至第一分馏塔作为其顶部进料。

4. 发明申请

US20110167868A1 HYDROCARBON GAS PROCESSING 有权
标题翻译：油气加工
公开(公告)号：US20110167868A1
公开(公告)日：2011-07-14
申请号：US12979563
申请日：2010-12-28
申请人： Michael C. Pierce , John D. Wilkinson , Hank M. Hudson
发明人： Michael C. Pierce , John D. Wilkinson , Hank M. Hudson
IPC分类号： F25J3/02
CPC分类号： F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J2200/04 , F25J2200/70 , F25J2200/72 , F25J2200/74 , F25J2200/78 , F25J2200/94 , F25J2205/04 , F25J2210/12 , F25J2230/30 , F25J2235/60 , F25J2240/02 , F25J2245/02 , F25J2270/12 , F25J2270/60
摘要： A process and an apparatus are disclosed for recovering ethane, ethylene, and heavier hydrocarbon components from a hydrocarbon gas stream. The stream is cooled, expanded to lower pressure, and supplied to a first fractionation tower at a mid-column feed position. A distillation liquid stream is withdrawn from the first fractionation tower below the feed position of the expanded stream, heated, and directed into a second fractionation tower that produces an overhead vapor stream and a bottom liquid stream. The overhead vapor stream is cooled to condense it, with a portion of the condensed stream directed to the second fractionation tower as its top feed and the remainder directed to the first fractionation tower at a lower column feed position. The bottom liquid stream from the second fractionation tower is cooled and directed to the first fractionation tower as its top feed.
摘要翻译：公开了从烃气流中回收乙烷，乙烯和较重烃组分的方法和装置。将料流冷却，膨胀至较低压力，并在中间柱进料位置供应至第一分馏塔。蒸馏液体流从第一分馏塔排出到膨胀物流的进料位置以下，被加热，并引导到产生顶部蒸汽流和底部液体物流的第二分馏塔中。将塔顶蒸气物流冷却以使其冷凝，一部分冷凝物流作为其顶部进料引导至第二分馏塔，其余部分以较低塔进料位置引导至第一分馏塔。将来自第二分馏塔的底部液体物流冷却并引导至第一分馏塔作为其顶部进料。

5. 发明授权

US5555748A Hydrocarbon gas processing 失效
标题翻译：烃类气体加工
公开(公告)号：US5555748A
公开(公告)日：1996-09-17
申请号：US477444
申请日：1995-06-07
申请人： Roy E. Campbell , John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
发明人： Roy E. Campbell , John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
IPC分类号： F25J3/02
CPC分类号： F25J3/0238 , F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0242 , F25J2200/02 , F25J2200/70 , F25J2205/04 , F25J2210/06 , F25J2210/12 , F25J2235/60 , F25J2240/02 , F25J2270/90
摘要： A process for the recovery of ethane, ethylene, propane, propylene and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed. The stream is cooled to partially condense it, then separated to provide a first vapor stream and a first condensed stream. The first vapor stream is divided into first and second streams, then the first stream is combined with the first condensed stream. The combined stream is cooled and expanded to an intermediate pressure to partially condense it, then separated to provide a second vapor stream and a second condensed stream. The second vapor stream is cooled at the intermediate pressure to condense substantially all of it and is thereafter expanded to the fractionation tower pressure and supplied to the fractionation tower at a top feed position. The second condensed stream is subcooled at the intermediate pressure, expanded to the tower pressure, and is supplied to the column at a first mid-column feed position. The second stream is expanded to the tower pressure and is then supplied to the column at a second mid-column feed position. The quantities and temperatures of the feeds to the column are effective to maintain the column overhead temperature at a temperature whereby the major portion of the desired components is recovered. In an alternative embodiment, the combined stream is cooled at essentially inlet pressure to partially condense it, then separated at pressure to provide the second vapor stream and the second condensed stream.
摘要翻译：公开了从烃气流中回收乙烷，乙烯，丙烷，丙烯和较重烃组分的方法。将物流冷却以部分地冷凝，然后分离以提供第一蒸气流和第一冷凝流。将第一蒸汽流分成第一和第二流，然后将第一流与第一冷凝流组合。将合并的流冷却并膨胀至中间压力以部分地冷凝，然后分离以提供第二蒸气流和第二冷凝流。第二蒸气流在中间压力下冷却，以基本上将其全部冷凝，然后膨胀至分馏塔压力，并在顶部进料位置供应至分馏塔。将第二冷凝物流在中间压力下过冷，膨胀至塔压力，并以第一中柱进料位置供应到塔中。将第二流扩张到塔压力，然后在第二中柱进料位置处供给塔。进料到塔的数量和温度对塔顶温度的维持是有效的，从而回收主要部分的所需组分。在替代实施例中，组合的流在基本入口压力下冷却以部分地冷凝，然后在压力下分离以提供第二蒸气流和第二冷凝流。

6. 发明授权

US06915662B2 Hydrocarbon gas processing 有权
标题翻译：烃类气体加工
公开(公告)号：US06915662B2
公开(公告)日：2005-07-12
申请号：US10003453
申请日：2001-10-26
申请人： John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
发明人： John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
IPC分类号： C07C7/00 , C10G5/06 , C10G70/04 , F25J3/02
CPC分类号： C10G70/04 , C07C7/005 , C10G5/06 , F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0238 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2200/90 , F25J2205/04 , F25J2210/12 , F25J2220/66 , F25J2235/60 , F25J2240/02 , F25J2245/02 , F25J2270/02 , F25J2290/40 , Y02C10/12
摘要： A process for the recovery of ethane, ethylene, propane, propylene and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed. In recent years, the preferred method of separating a hydrocarbon gas stream generally includes supplying at least portions of the gas stream to a fractionation tower having at least one reboiler, and often one or more side reboilers, to supply heat to the column by withdrawing and heating some of the tower liquids to produce stripping vapors that separate the more volatile components from the desired components. The reboiler and side reboilers (if any) are typically integrated into the feed stream cooling scheme to provide at least a portion of the refrigeration needed to condense the desired components for subsequent fractionation in the distillation column. In the process disclosed, the tower reboiling scheme is modified to use one or more tower liquid distillation streams from a point higher in the column than is used in the conventional reboiling scheme, providing colder stream(s) for the reboiler(s) that allow more effective cooling of the feed streams and thereby improve the efficiency with which the desired components are recovered. In addition, the tower liquid streams withdrawn from a higher point in the column contain larger quantities of the more volatile components, which when vaporized provide better stripping of undesirable components like carbon dioxide without reducing the recovery of the desired components. The heated distillation stream is returned to a lower point on the fractionation tower that is separated from the withdrawal point by at least one theoretical stage.
摘要翻译：公开了从烃气流中回收乙烷，乙烯，丙烷，丙烯和较重烃组分的方法。近年来，分离烃气流的优选方法通常包括将气流的至少一部分供应至具有至少一个再沸器的分馏塔，并且通常是一个或多个侧再沸器，以通过抽出和加热一些塔式液体以产生汽提蒸汽，其将更易挥发的组分与期望的组分分离。再沸器和侧面再沸器（如果有的话）通常集成到进料流冷却方案中，以提供冷凝所需组分所需的至少一部分制冷剂用于随后在蒸馏塔中分馏。在所公开的方法中，塔式再沸腾方案被修改为使用一种或多种塔式液体蒸馏物流，其比在常规再沸腾方案中使用的塔中高一点，为再沸器提供较冷的流，其允许更有效地冷却进料流，从而提高回收所需组分的效率。此外，从柱中较高点排出的塔液流含有较大量的挥发性较高的组分，当汽化时，会提供更好的汽提不需要的组分如二氧化碳，而不会降低所需组分的回收率。加热的蒸馏物流返回到分离塔上的一个较低点，其从提取点离开至少一个理论阶段。

7. 发明授权

US06182469B2 Hydrocarbon gas processing 有权
标题翻译：烃类气体加工
公开(公告)号：US06182469B2
公开(公告)日：2001-02-06
申请号：US09439508
申请日：1999-11-12
申请人： Roy E. Campbell , John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
发明人： Roy E. Campbell , John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
IPC分类号： F25J302
CPC分类号： F25J3/0233 , F25J3/0209 , F25J3/0219 , F25J3/0238 , F25J2200/02 , F25J2200/30 , F25J2200/70 , F25J2200/76 , F25J2200/90 , F25J2205/04 , F25J2210/12 , F25J2220/66 , F25J2235/60 , F25J2240/02 , F25J2245/02 , F25J2290/40 , Y02C10/12
摘要： A process for the recovery of ethane, ethylene, propane, propylene and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed. In recent years, the preferred method of separating a hydrocarbon gas stream generally includes supplying at least portions of the gas stream to a fractionation tower having at least one reboiler, and often one or more side reboilers, to supply heat to the column by withdrawing and heating some of the tower liquids to produce stripping vapors that separate the more volatile components from the desired components. The reboiler and side reboilers (if any) are typically integrated into the feed stream cooling scheme to provide at least a portion of the refrigeration needed to condense the desired components for subsequent fractionation in the distillation column. In the process disclosed, the tower reboiling scheme is modified to use one or more tower liquid distillation streams from a point higher in the column than is used in the conventional reboiling scheme, providing colder stream(s) for the reboiler(s) that allow more effective cooling of the feed streams and thereby improve the efficiency with which the desired components are recovered. In addition, the tower liquid streams withdrawn from a higher point in the column contain larger quantities of the more volatile components, which when vaporized provide better stripping of undesirable components like carbon dioxide without reducing the recovery of the desired components. The heated distillation stream is returned to a lower point on the fractionation tower that is separated from the withdrawal point by at least one theoretical stage.
摘要翻译：公开了从烃气流中回收乙烷，乙烯，丙烷，丙烯和较重烃组分的方法。近年来，分离烃气流的优选方法通常包括将气流的至少一部分供应至具有至少一个再沸器的分馏塔，并且通常是一个或多个侧再沸器，以通过抽出和加热一些塔式液体以产生汽提蒸汽，其将更易挥发的组分与期望的组分分离。再沸器和侧面再沸器（如果有的话）通常集成到进料流冷却方案中，以提供冷凝所需组分所需的至少一部分制冷剂用于随后在蒸馏塔中分馏。在所公开的方法中，塔式再沸腾方案被修改为使用一种或多种塔式液体蒸馏物流，其比在常规再沸腾方案中使用的塔中高一点，为再沸器提供较冷的流，其允许更有效地冷却进料流，从而提高回收所需组分的效率。此外，从柱中较高点排出的塔液流含有较大量的挥发性较高的组分，当汽化时，会提供更好的汽提不需要的组分如二氧化碳，而不会降低所需组分的回收率。加热的蒸馏物流返回到分离塔上的一个较低点，其从提取点离开至少一个理论阶段。

8. 发明授权

US5890378A Hydrocarbon gas processing 失效
标题翻译：烃类气体加工
公开(公告)号：US5890378A
公开(公告)日：1999-04-06
申请号：US52845
申请日：1998-03-31
申请人： C. L. Rambo , John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
发明人： C. L. Rambo , John D. Wilkinson , Hank M. Hudson , Michael C. Pierce
IPC分类号： C10G5/06 , C10L3/06 , F25J3/02 , F25J3/00
CPC分类号： C10L3/06 , C10G5/06 , F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/04 , F25J2200/70 , F25J2200/78 , F25J2205/02 , F25J2205/04 , F25J2210/06 , F25J2240/02 , F25J2270/02 , F25J2270/12 , F25J2270/60 , F25J2280/02 , F25J2290/40 , F25J2290/80
摘要： A process for the recovery of ethane, ethylene, propane, propylene and heavier hydrocarbon components from a hydrocarbon gas stream is disclosed. The stream is divided into first and second streams, and the second stream is cooled and expanded to a lower pressure and supplied to a contacting device. The first stream is cooled to condense substantially all of it, expanded to the lower pressure, and then used to cool a warmer distillation stream from a distillation column to at least partially condense the distillation stream. At least a portion of the partially condensed distillation stream is directed to the contacting device to intimately contact the expanded second stream, the resulting vapors and liquids are separated from the contacting device, and these liquids are supplied to the distillation column. The quantities and temperatures of the feeds to the contacting device and the distillation column are effective to maintain the overhead temperatures of the contacting device and the distillation column at temperatures whereby the major portion of the desired components is recovered.
摘要翻译：公开了从烃气流中回收乙烷，乙烯，丙烷，丙烯和较重烃组分的方法。将该流分成第一和第二流，并将第二流冷却并膨胀至较低压力并供应至接触装置。将第一流冷却至基本上将其全部冷凝，膨胀至较低的压力，然后用于冷却来自蒸馏塔的较热蒸馏物流至少部分冷凝蒸馏物流。部分冷凝的蒸馏物流的至少一部分被引导到接触装置以与膨胀的第二物流紧密接触，所得到的蒸气和液体与接触装置分离，并将这些液体供应到蒸馏塔。进料到接触装置和蒸馏塔的数量和温度有效地将接触装置和蒸馏塔的塔顶温度保持在温度，从而回收所需组分的主要部分。

9. 发明授权

US09939196B2 Hydrocarbon gas processing including a single equipment item processing assembly 有权
公开(公告)号：US09939196B2
公开(公告)日：2018-04-10
申请号：US12792136
申请日：2010-06-02
申请人： Andrew F. Johnke , W. Larry Lewis , John D. Wilkinson , Joe T. Lynch , Hank M. Hudson , Kyle T. Cuellar
发明人： Andrew F. Johnke , W. Larry Lewis , John D. Wilkinson , Joe T. Lynch , Hank M. Hudson , Kyle T. Cuellar
IPC分类号： F25J3/02
CPC分类号： F25J3/0209 , F25J3/0233 , F25J3/0266 , F25J3/0295 , F25J2200/02 , F25J2200/50 , F25J2200/74 , F25J2200/80 , F25J2205/04 , F25J2215/04 , F25J2235/80 , F25J2240/02 , F25J2240/40 , F25J2260/20 , F25J2260/80 , F25J2270/02 , F25J2270/90 , F25J2290/40 , Y02C10/12
摘要： A process and an apparatus are disclosed for a compact processing assembly to remove carbon dioxide from a hydrocarbon gas stream. The gas stream is cooled, expanded to intermediate pressure, and fed to the top of a mass transfer means. A distillation liquid stream from the mass transfer means is heated in a first heat and mass transfer means to strip out its volatile components and form a bottom liquid product. A distillation vapor stream from the mass transfer means is combined with any vapor in the expanded cooled gas stream, and the combined vapor stream is cooled in a second heat and mass transfer means to partially condense it, forming a condensed stream that is fed to the top of the mass transfer means. A portion of the bottom liquid product is subcooled, expanded to lower pressure, and used to cool the combined vapor stream.

10. 发明授权

US09068774B2 Hydrocarbon gas processing 有权
标题翻译：烃类气体加工
公开(公告)号：US09068774B2
公开(公告)日：2015-06-30
申请号：US13052575
申请日：2011-03-21
申请人： Andrew F. Johnke , W. Larry Lewis , L. Don Tyler , John D. Wilkinson , Joe T. Lynch , Hank M. Hudson , Kyle T. Cuellar
发明人： Andrew F. Johnke , W. Larry Lewis , L. Don Tyler , John D. Wilkinson , Joe T. Lynch , Hank M. Hudson , Kyle T. Cuellar
IPC分类号： F25J3/00 , F25J3/02
CPC分类号： F25J3/0209 , F25J3/0233 , F25J3/0238 , F25J3/0242 , F25J2200/02 , F25J2200/70 , F25J2200/74 , F25J2200/78 , F25J2200/80 , F25J2205/02 , F25J2205/04 , F25J2235/60 , F25J2240/02 , 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 C2 (or C3) 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加工组件以从烃气流中回收C2（或C3）组分和较重烃组分的方法和装置。将气流冷却并分成第一和第二流。第一流进一步冷却，膨胀至较低压力，并作为两个吸收装置之间的进料供应。将第二流膨胀到较低压力并作为底部进料供给到下部吸收装置。来自下部吸收装置的底部的蒸馏液体流在热和质量传递装置中被加热以除去其挥发性组分。来自热和质量传递装置的顶部的蒸馏蒸汽流由上吸收装置的顶部的蒸馏蒸气流冷却，从而形成作为顶部进料供应到上部吸收装置的冷凝流。

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