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公开(公告)号：US10046251B2
公开(公告)日：2018-08-14
申请号：US14853319
申请日：2015-09-14
CPC分类号： B01D3/20 , B01D3/22 , B01D3/324 , B01D3/326 , B01D3/4261 , F25J3/0209 , F25J3/0219 , F25J3/0233 , F25J3/0266 , F25J3/0295 , F25J2200/02 , F25J2200/30 , F25J2200/50 , F25J2200/74 , F25J2200/76 , F25J2200/90 , F25J2205/04 , F25J2205/20 , F25J2270/90 , F25J2280/02 , F25J2280/40 , Y02C10/12
摘要： An apparatus is disclosed for maintaining constant fluid pressure and equalized fluid flow among a plurality of downcomer lines through which liquid from a tower is directed. A substantially annular fluid distribution belt is disposed at the circumference of the tower. The fluid distribution belt collects liquid from the tower. At least two outlets direct liquid from the fluid distribution belt out of the tower and into a corresponding number of downcomer lines disposed external to the tower.
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22.发明申请公开(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：US09314715B2
公开(公告)日：2016-04-19
申请号：US14683854
申请日：2015-04-10
摘要： The current disclosure relates to multiphase fluid separation via a multiphase separation system. The multiphase separation system is configured to feed a multiphase fluid into feed lines within the multiphase separation system, wherein the feed lines consist of an upper line, a middle line, and a lower line. The upper line is configured to flow a first stream substantially including oil into an oil section of a control volume. The middle line is configured to flow a second stream substantially including an oil/water emulsion into an oil/water emulsion section of the control volume. The lower line is configured to flow a third stream substantially including water into a water section of the control volume. The control volume is configured to adjust fluid flow rate at an outlet, wherein the oil section, the water section, and the oil/water emulsion section each commingle at different heights of the control volume.
摘要翻译： 本公开涉及通过多相分离系统的多相流体分离。 多相分离系统被配置为将多相流体供给到多相分离系统内的进料管线中，其中进料管线由上部管线，中间管线和下部管线组成。 上部线被配置成将基本上包括油的第一流流入控制体积的油部分。 中间线被配置成将基本上包含油/水乳液的第二流流入控制体积的油/水乳液部分。 较低的线被配置成将基本上包括水的第三流流动到控制体积的水部分中。 控制体积被配置为调节出口处的流体流速，其中，油分段，水部分和油/水乳液部分各自在控制体积的不同高度处相交。
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24.发明申请公开(公告)号：US20150159944A1
公开(公告)日：2015-06-11
申请号：US14516689
申请日：2014-10-17
CPC分类号： F25J3/0266 , B01D3/4211 , C07C7/05 , C10L3/101 , C10L2290/141 , C10L2290/18 , C10L2290/36 , C10L2290/543 , C10L2290/58 , C10L2290/60 , F25J1/0022 , F25J1/0027 , F25J3/0209 , F25J3/0233 , F25J3/0295 , F25J3/061 , F25J3/0635 , F25J3/08 , F25J2200/02 , F25J2200/30 , F25J2200/50 , F25J2200/74 , F25J2205/04 , F25J2205/20 , F25J2220/66 , F25J2235/60 , F25J2280/02 , F25J2280/40 , F25J2290/12 , F25J2290/40 , Y02C10/12
摘要： The present disclosure provides a method for separating a feed stream in a distillation tower. The method may include forming solids in a controlled freeze zone section of the distillation tower; emitting radiation from a first radiation source in the controlled freeze zone section while the controlled freeze zone section forms no solids; detecting radiation emitted by the first radiation source as a first radiation level; detecting radiation emitted by the first radiation source as a second radiation level after detecting the first radiation level; and determining whether the solids adhered to at least one of on and around a first mechanical component included in the controlled freeze zone section based on the first radiation level and the second radiation level.
摘要翻译： 本公开提供了分离蒸馏塔中的进料流的方法。 该方法可以包括在蒸馏塔的受控冷冻区段中形成固体; 在控制的冻结区段中从第一辐射源发射辐射，而控制的冻结区段不形成固体; 检测由所述第一辐射源发射的辐射作为第一辐射水平; 在检测到第一辐射水平之后，检测由第一辐射源发射的辐射作为第二辐射水平; 以及基于所述第一辐射水平和所述第二辐射水平确定所述固体是否粘附在包含在所述受控冷冻区段中的第一机械部件的周围和周围中的至少一个上。
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25.发明申请In-Line Device for Gas-Liquid Contacting, and Gas Processing Facility Employing Co-Current Contactors 有权用于气液接触的在线装置和采用并流接触器的气体处理装置公开(公告)号：US20120238793A1
公开(公告)日：2012-09-20
申请号：US13189201
申请日：2011-07-22
CPC分类号： B01D19/0036 , B01D3/14 , B01D53/18 , B01D53/263 , B01D2252/2023 , B01D2256/24 , B01D2257/80 , C10L3/103 , C10L3/106
摘要： Provided are gas processing facilities for the separation of components in a gas stream and methods of using the same. The facility includes one or more co-current contactors. Each contactor includes a mass transfer vessel having a mixing section. The mixing section receives a gas stream and a liquid contacting stream. The mixing section mixes theses two streams and releases a two-phase flow. Each contactor also includes a separator that receives the two-phase fluid stream from the mass transfer vessel in-line, and then separates a vapor phase from a liquid phase. The separator has a gas-phase outlet configured to release the vapor phase as a treated gas stream, and a liquid-phase outlet configured to release the liquid phase as a loaded treating solution. The contactors may be used to remove water or other contaminant from a natural gas stream or other gas stream.
摘要翻译： 提供了用于分离气流中的组分的气体处理设备及其使用方法。 该设施包括一个或多个并流接触器。 每个接触器包括具有混合部分的传质容器。 混合部分接收气流和液体接触流。 混合部分混合这两个流并释放两相流。 每个接触器还包括分离器，其接收来自传质容器的两相流体流线，然后将气相与液相分离。 分离器具有构造成作为处理气流释放气相的气相出口，以及构造成作为负载处理溶液释放液相的液相出口。 接触器可用于从天然气流或其它气流中除去水或其它污染物。
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公开(公告)号：US20110168019A1
公开(公告)日：2011-07-14
申请号：US13119356
申请日：2009-08-27
IPC分类号： B01D53/14
CPC分类号： B01D53/1468 , B01D53/1406 , B01D53/1475 , B01D53/77 , B01D2251/206 , B01D2257/304 , B01D2257/504 , Y02C10/06
摘要： A gas processing facility for the separation of fluids is provided. The facility includes co-current contactors placed in series. Each co-current contactor receives a gas stream that includes a non-absorbing gas such as a hydrocarbon gas or nitrogen. The gas stream also includes an acid gas or other contaminant. Each co-current contactor also receives a liquid solvent stream. The co-current contactors then each release a sweetened gas stream and a gas-treating solution. In one processing direction, the contactors are arranged to deliver progressively sweetened gas streams. In the opposite processing direction, the contactors are arranged to deliver progressively richer gas-treating solutions. In one aspect, the facility includes at least a first co-current contactor, a second co-current contactor and a final co-current contactor. However, any number of at least two co-current separators may be employed. Methods and processes for separating a gas stream are also provided.
摘要翻译： 提供了用于分离流体的气体处理设备。 该设施包括串联的并流接触器。 每个并流接触器接收包括诸如烃气体或氮气的非吸收气体的气流。 气流还包括酸性气体或其它污染物。 每个并流接触器还接收液体溶剂流。 然后，共同电流接触器释放出增加的气流和气体处理溶液。 在一个处理方向上，接触器布置成递送逐渐变甜的气流。 在相反的处理方向上，接触器布置成递送更加丰富的气体处理溶液。 在一个方面，该设施包括至少第一并流接触器，第二并流接触器和最终并流接触器。 然而，可以使用任何数量的至少两个并流分离器。 还提供了用于分离气流的方法和方法。
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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：US10391442B2
公开(公告)日：2019-08-27
申请号：US15009936
申请日：2016-01-29
IPC分类号： B01D11/04 , B01D53/14 , B01D53/52 , B01D53/79 , C10L3/10 , B01D53/18 , B01D11/00 , C10G21/00
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：US09764252B2
公开(公告)日：2017-09-19
申请号：US14380589
申请日：2013-02-25
IPC分类号： B01D17/02 , B01D17/04 , B01D17/06 , B01D21/26 , B04C3/00 , B04C3/04 , B03C11/00 , C10G31/10 , E21B43/34
CPC分类号： B01D17/0217 , B01D17/045 , B01D17/06 , B01D21/267 , B03C11/00 , B04C3/04 , B04C2003/003 , B04C2003/006 , C10G31/10 , E21B43/34
摘要： A system and method for enhancing separation of a denser phase liquid from a lighter phase liquid within a multiphase stream. In one example, a cyclonic coalescer has a tubular housing and a plurality of coaxial flow chambers extending in the axial direction of the housing. A swirling element is associated with each of the plurality of coaxial flow chambers. The swirling elements are constructed and arranged to impart a tangential velocity of the stream flowing through the associated flow chamber.
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