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公开(公告)号:US20170145803A1
公开(公告)日:2017-05-25
申请号:US15262036
申请日:2016-09-12
CPC分类号: E21B43/36 , B01D53/1425 , B01D53/1462 , B01D53/1493 , B01D53/18 , B01D53/263 , B01D53/28 , B01D2252/2023 , B01D2252/2026 , B01D2256/245 , B01D2257/80 , C10L3/103 , C10L3/104 , C10L3/106 , C10L2290/12 , C10L2290/46 , C10L2290/541 , C10L2290/542 , C10L2290/545 , C10L2290/56 , Y02C10/06
摘要: Systems and methods for dehydrating a natural gas stream are provided herein. The system includes a lean solvent feed system, including a line from a topsides facility, wherein the line is configured to divide a lean solvent stream to feed lean solvent to each of a number of co-current contacting systems in parallel. The co-current contacting systems are placed in series along a wet natural gas stream, wherein each of the co-current contacting systems is configured to contact the lean solvent stream with the wet natural gas stream to adsorb at least a portion of the water from the wet natural gas stream to form a dry natural gas stream. A rich solvent return system includes a line to combine rich solvent from each of the plurality of co-current contacting systems and return a rich solvent stream to the topsides facility.
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公开(公告)号:US20180362858A1
公开(公告)日:2018-12-20
申请号:US15950867
申请日:2018-04-11
摘要: A hydrogen sulfide (H2S) scavenging system for removing H2S, mercaptans, and/or other sulfur-containing compounds from a natural gas stream. A co-current contacting system is located in-line within a pipe and receives the natural gas stream and a liquid scavenger stream. The co-current contacting system includes a co-current contactor including a droplet generator and a mass transfer section. The droplet generator generates droplets from the liquid scavenger stream and disperses the droplets into the natural gas stream. The mass transfer section provides a mixed, two-phase flow having a vapor phase and a liquid phase. The liquid phase includes the liquid scavenger stream with H2S, mercaptans, and/or other sulfur-containing compounds absorbed from the natural gas stream, and the vapor phase includes the natural gas stream. A separation system separates the vapor phase from the liquid phase.
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公开(公告)号:US10040022B2
公开(公告)日:2018-08-07
申请号:US15284973
申请日:2016-10-04
申请人: Tracy A. Fowler , Shwetha Ramkumar , Jeffrey W. Frederick , Ananda K. Nagavarapu , Sebastian Chialvo , Robert F. Tammera , John W. Fulton
发明人: Tracy A. Fowler , Shwetha Ramkumar , Jeffrey W. Frederick , Ananda K. Nagavarapu , Sebastian Chialvo , Robert F. Tammera , John W. Fulton
IPC分类号: B01D53/04 , B01D53/047
摘要: Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to remove contaminants, such as water, from the stream. As part of the process, the adsorbent bed unit may include additional space for the valves of the adsorbent bed unit.
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公开(公告)号:US20170113175A1
公开(公告)日:2017-04-27
申请号:US15284960
申请日:2016-10-04
申请人: Tracy A. Fowler , Shwetha Ramkumar , Jeffrey W. Frederick , Ananda K. Nagavarapu , Sebastian Chialvo , Robert F. Tammera , John W. Fulton
发明人: Tracy A. Fowler , Shwetha Ramkumar , Jeffrey W. Frederick , Ananda K. Nagavarapu , Sebastian Chialvo , Robert F. Tammera , John W. Fulton
IPC分类号: B01D53/04
CPC分类号: B01D53/0446 , B01D53/0462 , B01D53/0473 , B01D2256/245 , B01D2257/504 , B01D2257/702 , B01D2257/80 , B01D2259/40003 , B01D2259/40086
摘要: Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to remove contaminants, such as water, from the stream. As part of the process, the adsorbent bed unit may include additional space for the valves on the head of the adsorbent bed unit.
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公开(公告)号:US11260342B2
公开(公告)日:2022-03-01
申请号:US15949613
申请日:2018-04-10
摘要: A fractionation system for removing heavy hydrocarbons in a gas stream. A stripping section receives a predominantly liquid phase of the feed gas stream. A co-current contacting system receives a predominantly vapor phase of the feed gas stream. The co-current contacting system includes a compact contacting bundle disposed within a vessel and including a plurality of substantially parallel contacting units, each of the plurality of contacting units having a droplet generator, a mass transfer section, and a separation system. Each droplet generator generates droplets from a liquid disperses the droplets into a gas stream. Each mass transfer section provides a mixed, two-phase flow having a vapor phase and a liquid phase. Each separation system separates the vapor phase from the liquid phase such that the concentration of heavy hydrocarbons in the vapor phase is lower than in the liquid phase.
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公开(公告)号:US11000795B2
公开(公告)日:2021-05-11
申请号:US15964866
申请日:2018-04-27
摘要: A fractionation system for removing heavy hydrocarbons in a gas stream. A stripping section receives a predominantly liquid phase of a feed gas stream. First and second co-current contacting systems are located in-line within a pipe. The first co-current contacting system receives a predominantly vapor phase of the feed gas stream. Each co-current contacting system includes a co-current contactor and a separation system. Each co-current contactor includes a droplet generator and a mass transfer section. The droplet generator generates droplets from a liquid and disperses the droplets into a gas stream. The mass transfer section provides a mixed, two-phase flow having a vapor phase and a liquid phase. The separation system separates the vapor phase from the liquid phase.
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公开(公告)号:US10322365B2
公开(公告)日:2019-06-18
申请号:US15284960
申请日:2016-10-04
申请人: Tracy A. Fowler , Shwetha Ramkumar , Jeffrey W. Frederick , Ananda K. Nagavarapu , Sebastian Chialvo , Robert F. Tammera , John W. Fulton
发明人: Tracy A. Fowler , Shwetha Ramkumar , Jeffrey W. Frederick , Ananda K. Nagavarapu , Sebastian Chialvo , Robert F. Tammera , John W. Fulton
IPC分类号: B01D53/04 , B01D53/047
摘要: Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to remove contaminants, such as water, from the stream. As part of the process, the adsorbent bed unit may include additional space for the valves on the head of the adsorbent bed unit.
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公开(公告)号:US20170113176A1
公开(公告)日:2017-04-27
申请号:US15284973
申请日:2016-10-04
申请人: Tracy A. Fowler , Shwetha Ramkumar , Jeffrey W. Frederick , Ananda K. Nagavarapu , Sebastian Chialvo , Robert F. Tammera , John W. Fulton
发明人: Tracy A. Fowler , Shwetha Ramkumar , Jeffrey W. Frederick , Ananda K. Nagavarapu , Sebastian Chialvo , Robert F. Tammera , John W. Fulton
IPC分类号: B01D53/04
CPC分类号: B01D53/0446 , B01D53/0462 , B01D53/047 , B01D53/0473 , B01D2256/245 , B01D2257/504 , B01D2257/702 , B01D2257/80 , B01D2259/40003 , B01D2259/40086 , Y02C10/08
摘要: Provided are apparatus and systems for performing a swing adsorption process. This swing adsorption process may involve passing streams through adsorbent bed units to remove contaminants, such as water, from the stream. As part of the process, the adsorbent bed unit may include additional space for the valves of the adsorbent bed unit.
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公开(公告)号:US20180361307A1
公开(公告)日:2018-12-20
申请号:US15964866
申请日:2018-04-27
摘要: A fractionation system for removing heavy hydrocarbons in a gas stream. A stripping section receives a predominantly liquid phase of a feed gas stream. First and second co-current contacting systems are located in-line within a pipe. The first co-current contacting system receives a predominantly vapor phase of the feed gas stream. Each co-current contacting system includes a co-current contactor and a separation system. Each co-current contactor includes a droplet generator and a mass transfer section. The droplet generator generates droplets from a liquid and disperses the droplets into a gas stream. The mass transfer section provides a mixed, two-phase flow having a vapor phase and a liquid phase. The separation system separates the vapor phase from the liquid phase.
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公开(公告)号:US20180361309A1
公开(公告)日:2018-12-20
申请号:US15949613
申请日:2018-04-10
摘要: A fractionation system for removing heavy hydrocarbons in a gas stream. A stripping section receives a predominantly liquid phase of the feed gas stream. A co-current contacting system receives a predominantly vapor phase of the feed gas stream. The co-current contacting system includes a compact contacting bundle disposed within a vessel and including a plurality of substantially parallel contacting units, each of the plurality of contacting units having a droplet generator, a mass transfer section, and a separation system. Each droplet generator generates droplets from a liquid disperses the droplets into a gas stream. Each mass transfer section provides a mixed, two-phase flow having a vapor phase and a liquid phase. Each separation system separates the vapor phase from the liquid phase such that the concentration of heavy hydrocarbons in the vapor phase is lower than in the liquid phase.
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