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公开(公告)号:US20160236140A1
公开(公告)日:2016-08-18
申请号:US15004348
申请日:2016-01-22
摘要: A co-current contactor for separating components in a fluid stream, the co-current contactor comprising a first inlet configured to receive the fluid stream proximate to a first end of the co-current contactor, a second inlet configured to receive a solvent proximate the first end of the co-current contactor, and a mass transfer section configured to receive the fluid stream and the solvent and to provide a mixed, two-phase flow, wherein the mass transfer section comprises a surface feature along an inner surface of the mass transfer section configured to reduce film flow along an inner wall of the mass transfer section, and wherein the surface feature comprises at least one of a hydrophobic surface, a superhydrophobic surface, a porous wall surface, and a nonlinear surface irregularity extending radially inward or radially outward along the inner surface of the mass transfer section.
摘要翻译: 用于分离流体流中的组分的并流接触器,所述并流接触器包括被配置为接收靠近所述并流接触器的第一端的所述流体流的第一入口,被配置为接收所述流体流附近的溶剂的第二入口 并流式接触器的第一端和被配置为接收流体流和溶剂并且提供混合的两相流的传质部分,其中质量传递部分包括沿着质量的内表面的表面特征 传送部分,其构造成减小沿着传质部分的内壁的膜流动,并且其中所述表面特征包括疏水表面,超疏水表面,多孔壁表面和径向向内或径向延伸的非线性表面不规则中的至少一个 沿着传质部分的内表面向外延伸。
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公开(公告)号:US10717039B2
公开(公告)日:2020-07-21
申请号:US15004348
申请日:2016-01-22
摘要: A co-current contactor for separating components in a fluid stream, the co-current contactor comprising a first inlet configured to receive the fluid stream proximate to a first end of the co-current contactor, a second inlet configured to receive a solvent proximate the first end of the co-current contactor, and a mass transfer section configured to receive the fluid stream and the solvent and to provide a mixed, two-phase flow, wherein the mass transfer section comprises a surface feature along an inner surface of the mass transfer section configured to reduce film flow along an inner wall of the mass transfer section, and wherein the surface feature comprises at least one of a hydrophobic surface, a superhydrophobic surface, a porous wall surface, and a nonlinear surface irregularity extending radially inward or radially outward along the inner surface of the mass transfer section.
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3.
公开(公告)号:US20180071674A1
公开(公告)日:2018-03-15
申请号:US15652856
申请日:2017-07-18
IPC分类号: B01D53/14
CPC分类号: B01D53/1412 , B01D53/1462 , B01D53/1468 , B01D53/1475 , B01D53/1493 , B01D2252/20405 , B01D2252/20431 , B01D2252/20489 , B01D2257/302 , B01D2257/304 , B01D2257/306 , B01D2257/308 , B01D2257/504 , Y02C10/06
摘要: Systems and methods for separating CO2 and H2S from a gaseous stream are provided herein. The system includes a selective solvent that is utilized with a compact contacting technology unit to remove H2S from a gaseous stream.
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公开(公告)号:US20190336908A1
公开(公告)日:2019-11-07
申请号:US16513156
申请日:2019-07-16
IPC分类号: B01D53/14 , B01D53/18 , C10L3/10 , B01D53/52 , B01D53/79 , C10G21/16 , C10G21/30 , C10G70/06 , B01D11/04
摘要: The disclosure includes a method, comprising passing a fluid into a co-current contactor, passing a solvent into the co-current contactor, dividing the solvent into solvent droplets having a first average droplet size, placing the fluid in contact with the solvent droplets to create a combined stream, coalescing at least a portion of the solvent droplets to create solvent droplets having a second average droplet size, wherein the second average droplet size is greater than the first average droplet size, and separating the fluid and the solvent.
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公开(公告)号:US20160263516A1
公开(公告)日:2016-09-15
申请号:US15009936
申请日:2016-01-29
CPC分类号: B01D53/1406 , B01D11/04 , B01D11/0419 , B01D11/0488 , B01D53/1462 , B01D53/18 , B01D53/526 , B01D53/79 , B01D2011/005 , B01D2252/204 , B01D2257/304 , B01D2257/504 , C10G21/00 , C10G21/16 , C10G21/30 , C10G70/06 , C10G2300/207 , C10L3/10 , C10L3/103 , C10L3/104 , C10L2290/18 , C10L2290/541
摘要: The disclosure includes a method, comprising passing a fluid into a co-current contactor, passing a solvent into the co-current contactor, dividing the solvent into solvent droplets having a first average droplet size, placing the fluid in contact with the solvent droplets to create a combined stream, coalescing at least a portion of the solvent droplets to create solvent droplets having a second average droplet size, wherein the second average droplet size is greater than the first average droplet size, and separating the fluid and the solvent.
摘要翻译: 本公开包括一种方法,包括使流体流入并流接触器,将溶剂通入并流接触器,将溶剂分成具有第一平均液滴尺寸的溶剂液滴,使流体与溶剂液滴接触 产生组合的流,将至少一部分溶剂液滴聚结以产生具有第二平均液滴尺寸的溶剂液滴,其中第二平均液滴尺寸大于第一平均液滴尺寸,并分离流体和溶剂。
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公开(公告)号:US11000797B2
公开(公告)日:2021-05-11
申请号:US16102297
申请日:2018-08-13
摘要: A method of separating impurities from a natural gas stream. The natural gas stream is cooled through heat exchange with one or more process streams to produce a chilled gas stream, which is contacted with a lean solvent stream in a contactor to separate hydrogen sulfide (H2S) from the chilled gas stream, thereby producing a rich solvent stream and a partially-treated gas stream. Carbon dioxide (CO2) and H2S are separated from the partially-treated gas stream in a membrane separation system, thereby creating a fully-treated gas stream and a permeate gas stream, the permeate gas stream being comprised primarily of H2S and CO2, and the fully-treated gas stream being comprised primarily of natural gas. The fully-treated gas stream and the permeate gas stream are at a lower temperature than the partially-treated gas stream. The fully-treated gas stream and the permeate gas stream comprise the one or more process streams.
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公开(公告)号:US20190054415A1
公开(公告)日:2019-02-21
申请号:US16102278
申请日:2018-08-13
摘要: A method of separating impurities from a natural gas stream. CO2 and H2S are separated from the natural gas stream in a membrane separation system, thereby creating a partially-treated gas stream and a permeate gas stream, both of which are at a lower temperature than the natural gas stream. The partially-treated gas stream is contacted with a first lean solvent stream in a first contactor to separate H2S from the partially-treated gas stream, thereby producing a first rich solvent stream and a fully-treated gas stream. The permeate gas stream is contacted with a second lean solvent stream in a second contactor to separate H2S therefrom to produce a second rich solvent stream and a CO2 gas stream. H2S and CO2 are removed from the first and second rich solvent streams, thereby producing the first and second lean solvent streams.
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公开(公告)号:US20170239612A1
公开(公告)日:2017-08-24
申请号:US15436203
申请日:2017-02-17
申请人: Suhas P. Mondkar , P. Scott Northrop , Jenny P. Seagraves , Ransdall K. Smith , Shwetha Ramkumar
发明人: Suhas P. Mondkar , P. Scott Northrop , Jenny P. Seagraves , Ransdall K. Smith , Shwetha Ramkumar
CPC分类号: B01D53/1468 , B01D53/1406 , B01D53/1475 , B01D53/1493 , B01D2252/20426 , B01D2252/20431 , B01D2252/20478 , B01D2256/245 , B01D2257/304 , C10L3/103 , C10L3/104 , C10L2290/541 , C10L2290/543 , F25J3/0209 , F25J3/08 , F25J2220/66
摘要: A method of removing impurities from a natural gas stream. A selective solvent is provided that absorbs a first impurity at a first rate and a second impurity at a second rate that is slower than the first rate. The solvent is cooled to a temperature below 60° F. to provide a cooled solvent. The cooled solvent is contacted with the natural gas stream, thereby generating a rich solvent that includes the first impurity. The rich solvent is removed from the natural gas stream, wherein an amount of the first impurity remaining in the natural gas stream is below a sales gas requirement.
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公开(公告)号:US09739529B2
公开(公告)日:2017-08-22
申请号:US14700993
申请日:2015-04-30
CPC分类号: F25J3/0214 , F25J3/0209 , F25J3/0233 , F25J3/0266 , F25J3/0295 , F25J2200/02 , F25J2200/30 , F25J2200/50 , F25J2200/74 , F25J2205/04 , F25J2205/20 , F25J2210/62 , F25J2235/60 , F25J2245/02 , F25J2280/10 , F25J2280/40 , F25J2290/40 , F25J2290/62 , Y02C10/12
摘要: A method and system for separating fluids in a distillation tower. The method may include feeding a stream to the distillation tower, wherein the stream includes carbon dioxide, reducing a carbon dioxide concentration of the stream received by the rectifier section by feeding a first cryogenic fluid to the controlled freeze zone section and accumulating rectifier section stream in at least one of a holding vessel and a sump of the rectifier section, and terminating reducing the carbon dioxide concentration when the carbon dioxide concentration of the stream travelling from the controlled freeze zone section to the rectifier section is less than or equal to a maximum carbon dioxide concentration. The first cryogenic fluid may comprise a substantially carbon-dioxide-free fluid.
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10.
公开(公告)号:US20170080385A1
公开(公告)日:2017-03-23
申请号:US15219882
申请日:2016-07-26
申请人: P. Scott Northrop
发明人: P. Scott Northrop
CPC分类号: B01D53/52 , B01D53/1418 , B01D53/8612 , B01D2251/102 , B01D2251/602 , B01D2255/10 , B01D2255/20707 , B01D2256/22 , B01D2257/304 , C01B17/0404 , C01B17/48 , C09K8/594 , E21B43/40
摘要: Systems and methods for separating hydrogen sulfide from carbon dioxide in a high-pressure mixed stream are disclosed herein. The methods include receiving the high-pressure mixed stream in an oxidation reactor and at an inlet pressure of at least 0.3 megapascals. The high-pressure mixed stream includes 0.01 to 5 mole percent hydrogen sulfide and at least 90 mole percent carbon dioxide. The methods further include oxidizing the high-pressure mixed stream with an oxidant to generate a high-pressure oxidized stream, includes oxidized hydrogen sulfide and carbon dioxide, at an oxidation pressure of at least 0.3 megapascals. The methods also include separating the high-pressure oxidized stream into an oxidized hydrogen sulfide product and a carbon dioxide product and generating the carbon dioxide product at a pressure of at least 0.3 megapascals. The systems include the high-pressure mixed stream, an oxidation reactor, and a separation assembly.
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