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1. 发明申请

WO2011034666A2 APPARATUS AND PROCESS FOR ISOMERIZING A HYDROCARBON STREAM 审中-公开
标题翻译：用于使烃流异构化的装置和方法
公开(公告)号：WO2011034666A2
公开(公告)日：2011-03-24
申请号：PCT/US2010/044552
申请日：2010-08-05
申请人： UOP LLC , GARNEY, Bryan, S. , DAGUIO, Jocelyn, C. , DETRICK, Kurt, A. , SHECTERLE, David, J. , KRUPCZAK, John, M. , MEZERA, Andrew, D. , BECCI, Douglas, A.
发明人： GARNEY, Bryan, S. , DAGUIO, Jocelyn, C. , DETRICK, Kurt, A. , SHECTERLE, David, J. , KRUPCZAK, John, M. , MEZERA, Andrew, D. , BECCI, Douglas, A.
IPC分类号： C07C5/22 , C07C7/04 , C07B35/08 , C10G45/58
CPC分类号： C10G45/58
摘要： An apparatus and process for isomerizing a hydrocarbon stream rich in a C4 and/or a C5 and C6 hydrocarbon which includes a first and a second drier; and a reaction zone communicating with at least the first drier. The first drier operates at a first condition to dry the reactant and the second drier operates at a second condition during regeneration. The used regenerant remaining in the second drier after regeneration can (1) pass through a vent-to-flare assembly in a batch-wise manner; (2) pass through a downflow-depressure-to-low-pressure-device assembly in a batch-wise manner; (3) pass through a cross-over piping purge assembly to minimize upsets in the reaction and fractionation zones when the second drier is placed back in operation; or any combination of (1) (2) and/or (3) to minimize upsets in the reaction and fractionation zones when the second drier is placed back in operation.
摘要翻译：一种用于使富含C4和/或C5和C6烃的烃流异构化的装置和方法，所述烃流包括第一和第二干燥器; 以及与至少第一干燥器连通的反应区。第一干燥器在第一条件下操作以干燥反应物并且第二干燥器在再生期间在第二条件下操作。在再生之后保留在第二干燥器中的用过的再生剂可以（1）以分批的方式通过通风 - 火炬组件; （2）以分批方式通过降流 - 降压 - 低压装置组件; （3）通过交叉管道吹扫组件，以在第二干燥器重新投入运行时使反应区和分馏区的干扰最小化; 或（1）（2）和/或（3）的任何组合以使第二干燥器重新投入运行时反应区和分馏区中的干扰最小化。

2. 发明申请

WO2006099078A3 HIGH FLUX, MICROPOROUS, SIEVING MEMBRANES AND SEPARATORS CONTAINING SUCH MEMBRANES AND PROCESSES USING SUCH MEMBRANES 审中-公开
公开(公告)号：WO2006099078A3
公开(公告)日：2006-09-21
申请号：PCT/US2006/008478
申请日：2006-03-10
申请人： UOP LLC , KULPRATHIPANJA, Santi , LIU, Chunqing , WILSON, Stephen T. , LESCH, David A. , RICE, Lynn H. , SHECTERLE, David J. , SHIELDS, Dale J. , FREY, Stanley J.
发明人： KULPRATHIPANJA, Santi , LIU, Chunqing , WILSON, Stephen T. , LESCH, David A. , RICE, Lynn H. , SHECTERLE, David J. , SHIELDS, Dale J. , FREY, Stanley J.
IPC分类号： A61F2/00 , A61K9/24
摘要： A sieving membrane comprises a thin, microporous barrier to provide a high flux. The membrane structure can tolerate defects yet still obtain commercially-attractive separations.

3. 发明申请

WO2013147787A1 PROCESS FOR CONTROLLING A TEMPERATURE IN AN ISOMERIZATION ZONE 审中-公开
标题翻译：控制异构化区温度的方法
公开(公告)号：WO2013147787A1
公开(公告)日：2013-10-03
申请号：PCT/US2012/031138
申请日：2012-03-29
申请人： UOP LLC , SHECTERLE, David J.
发明人： SHECTERLE, David J.
IPC分类号： B01J19/00 , C07C5/22 , C07C7/148 , C07C7/20 , B01J19/24
CPC分类号： B01J19/242 , B01J2219/00103 , C07C5/277 , C07C2521/04 , C07C2521/06 , C07C2523/42 , C10G45/72 , C10G65/043 , C07C9/10 , C07C9/16
摘要： One exemplary embodiment can be a process for controlling a temperature in an isomerization zone. The process can include passing respective feeds through a first, a second, and a third isomerization reactors. Usually, a portion of an effluent from the first and second isomerization reactors is passed through respective exchangers to control the temperature in downstream reactors.
摘要翻译：一个示例性实施方案可以是用于控制异构化区域中的温度的方法。该方法可以包括使相应的进料通过第一，第二和第三异构化反应器。通常，来自第一和第二异构化反应器的流出物的一部分通过相应的交换器以控制下游反应器中的温度。

4. 发明申请

WO2010147819A3 APPARATUS AND PROCESS FOR ISOMERIZING A HYDROCARBON STREAM 审中-公开
公开(公告)号：WO2010147819A3
公开(公告)日：2010-12-23
申请号：PCT/US2010/037932
申请日：2010-06-09
申请人： UOP LLC , SHECTERLE, David, J. , GARNEY, Bryan, S. , DAGUIO, Jocelyn, C. , SHAWLEY, James, M.
发明人： SHECTERLE, David, J. , GARNEY, Bryan, S. , DAGUIO, Jocelyn, C. , SHAWLEY, James, M.
IPC分类号： C07C5/22 , C07B37/08 , C07C7/04 , C10G35/06
摘要： One exemplary embodiment can be an apparatus for isomerizing a hydrocarbon stream rich in a C4 hydrocarbon and/or at least one of a C5 and C6 hydrocarbon. The apparatus can include: a first drier and a second drier adapted to receive a fluid including at least one reactant; and a reaction zone communicating with the first drier to receive the fluid including at least one reactant and with the second drier to receive the regenerant. Generally, the first drier operates at a first condition to dry the fluid including at least one reactant and the second drier operates at a second condition during regeneration with a regenerant. The regenerant can pass through a fluid tapering device for regulating the flow of the regenerant to the reaction zone.

5. 发明申请

WO2006099078A2 HIGH FLUX, MICROPOROUS, SIEVING MEMBRANES AND SEPARATORS CONTAINING SUCH MEMBRANES AND PROCESSES USING SUCH MEMBRANES 审中-公开
标题翻译：高通量，微孔，切割膜和分离器，这些膜和使用这种膜的方法
公开(公告)号：WO2006099078A2
公开(公告)日：2006-09-21
申请号：PCT/US2006008478
申请日：2006-03-10
申请人： UOP LLC , KULPRATHIPANJA SANTI , LIU CHUNQING , WILSON STEPHEN T , LESCH DAVID A , RICE LYNN H , SHECTERLE DAVID J , SHIELDS DALE J , FREY STANLEY J
发明人： KULPRATHIPANJA SANTI , LIU CHUNQING , WILSON STEPHEN T , LESCH DAVID A , RICE LYNN H , SHECTERLE DAVID J , SHIELDS DALE J , FREY STANLEY J
IPC分类号： B01D61/00
CPC分类号： B01D71/028 , B01D67/0002 , B01D67/0006 , B01D67/0039 , B01D67/0041 , B01D67/0044 , B01D67/0046 , B01D67/0051 , B01D67/0072 , B01D69/10 , B01D69/141 , B01D71/021 , B01D71/027 , B01D71/64 , B01D2323/40 , B01D2325/02 , B01D2325/28 , C07C7/144 , C10G31/11 , Y02P20/582 , C07C15/08 , C07C9/14
摘要： A sieving membrane comprises a thin, microporous barrier to provide a high flux. The membrane structure can tolerate defects yet still obtain commercially-attractive separations.
摘要翻译：筛分膜包括薄的微孔屏障以提供高通量。膜结构可以容忍缺陷，但仍然获得商业上有吸引力的分离。

6. 发明申请

WO2012097051A1 PROCESS FOR ISOMERIZING A FEED STREAM INCLUDING ONE OR MORE C4-C6 HYDROCARBONS 审中-公开
标题翻译：含有一个或多个C4-C6烃的进料流的同位素方法
公开(公告)号：WO2012097051A1
公开(公告)日：2012-07-19
申请号：PCT/US2012/020919
申请日：2012-01-11
申请人： UOP LLC , SHECTERLE, David J.
发明人： SHECTERLE, David J.
IPC分类号： C07C5/13 , B01J21/06 , B01J19/24 , C07B61/00
CPC分类号： C10G45/62 , C10G2300/104 , C10G2300/305 , C10G2400/02
摘要： One exemplary embodiment can be a process for isomerizing a feed stream including one or more C4-C6 hydrocarbons. Generally, the process includes contacting the feed stream in an isomerization reaction zone with an isomerization catalyst at isomerization conditions to produce an isomerization zone effluent; passing at least a portion of the isomerization zone effluent to a stabilizer zone and recovering a stabilizer overhead stream, a bottom stream, and a side-stream; passing at least a portion of the side-stream to a stripper zone; and sending a stripper bottom stream to a C5 splitter zone and passing a stream from the C5 splitter zone to the isomerization reaction zone.
摘要翻译：一个示例性实施方案可以是使包含一种或多种C 4 -C 6烃的进料流异构化的方法。通常，该方法包括使异构化反应区中的进料流与异构化催化剂在异构化条件下接触以产生异构化区流出物; 将至少一部分异构化区流出物通入稳定剂区并回收稳定剂塔顶流，底部流和侧流; 将至少一部分侧流通入汽提区; 并将汽提塔底部流送到C5分流器区域，并将流从C5分流器区域传递到异构化反应区域。

7. 发明申请

WO2010147813A2 APPARATUS AND PROCESS FOR ISOMERIZING A HYDROCARBON STREAM 审中-公开
标题翻译：用于同化烃流的装置和方法
公开(公告)号：WO2010147813A2
公开(公告)日：2010-12-23
申请号：PCT/US2010/037885
申请日：2010-06-09
申请人： UOP LLC , SHECTERLE, David J. , GARNEY, Bryan S. , SHAWLEY, James M. , DAGUIO, Jocelyn C.
发明人： SHECTERLE, David J. , GARNEY, Bryan S. , SHAWLEY, James M. , DAGUIO, Jocelyn C.
IPC分类号： C07C5/22 , C07B37/08 , C10G35/06
CPC分类号： C10G35/04 , B01J2219/00006 , B01J2219/0004 , C10G45/58 , C10G2300/4081
摘要： One exemplary embodiment can be an apparatus for isomerizing a hydrocarbon stream rich in a C4 hydrocarbon and/or at least one of a C5 and C6 hydrocarbon. The apparatus can include: a vessel containing a fluid including at least one reactant; a fluid transfer device receiving the fluid including at least one reactant from the vessel; at least one drier receiving the fluid including at least one reactant from the fluid transfer device; and a reactor communicating with the at least one drier to receive the fluid including at least one reactant. In addition, the at least one drier may communicate with the vessel at least by sending the fluid including at least one reactant or the regenerant through a fluid tapering device for at least one of regulating the flow and reducing the pressure of the regenerant to the vessel.
摘要翻译：一个示例性实施方案可以是用于异构化富含C 4烃和/或C 5和C 6烃中的至少一种的烃流的装置。该装置可以包括：容器，其容纳包含至少一种反应物的流体; 流体输送装置，其从所述容器接收包含至少一种反应物的流体; 至少一个干燥器，其接收包括来自所述流体转移装置的至少一种反应物的流体; 以及与所述至少一个干燥器连通以接收包含至少一种反应物的流体的反应器。此外，至少一个干燥器可以至少通过使包含至少一种反应物或再生剂的流体通过流体锥形装置与容器连通，用于调节流动并将再生剂的压力降低到容器中的至少一种。

8. 发明申请

WO2012097041A1 PROCESS FOR ISOMERIZING A FEED STREAM INCLUDING ONE OR MORE C4-C6 HYDROCARBONS 审中-公开
标题翻译：含有一个或多个C4-C6烃的进料流的同位素方法
公开(公告)号：WO2012097041A1
公开(公告)日：2012-07-19
申请号：PCT/US2012/020899
申请日：2012-01-11
申请人： UOP LLC , SHECTERLE, David J.
发明人： SHECTERLE, David J.
IPC分类号： C07C5/27 , C07C9/14 , C07C7/20 , B01J23/42
CPC分类号： C07C5/2754 , C10G45/62 , C10G2300/104 , C10G2300/305 , C10G2400/02
摘要： One embodiment is a process for isomerizing a feed stream including one or more C4-C6 hydrocarbons including contacting the feed stream in an isomerization reaction zone with an isomerization catalyst at isomerization conditions to produce an isomerization zone effluent; passing at least a portion of the isomerization zone effluent to a stabilizer zone and recovering a stabilizer overhead stream, a bottom stream, and a stripper feed stream; passing the stripper feed stream to a stripping zone and separating the stripper feed stream into a stripper overhead stream and a stripper bottom stream; and recycling at least a portion of the stripper bottom stream to a deisopentanizer zone and passing a stream from the deisopentanizer zone to the isomerization reaction zone.
摘要翻译：一个实施方案是使包含一种或多种C 4 -C 6烃的进料流异构化的方法，包括使异构化反应区中的进料流与异构化催化剂在异构化条件下接触以产生异构化区流出物; 将至少一部分异构化区流出物通入稳定剂区并回收稳定剂塔顶流，底部流和汽提塔进料流; 将汽提器进料流通入汽提区，并将汽提塔进料流分离成脱气塔顶馏出物流和汽提塔塔底物流; 以及将至少一部分汽提塔底部料流再循环到去异戊烷化器区域，并将来自脱硫烷化器区域的物流传递到异构化反应区域。

9. 发明申请

WO2010144190A3 METHODS AND SYSTEMS FOR EFFICIENT NEUTRALIZATION OF ACID GASES 审中-公开
标题翻译：有效地中和酸性气体的方法和系统
公开(公告)号：WO2010144190A3
公开(公告)日：2011-03-31
申请号：PCT/US2010033501
申请日：2010-05-04
申请人： UOP LLC , BULLEN PATRICK J , SHECTERLE DAVID J , DAGUIO JOCELYN C
发明人： BULLEN PATRICK J , SHECTERLE DAVID J , DAGUIO JOCELYN C
IPC分类号： B01D53/34 , B01D53/40 , B01D53/78
CPC分类号： B01D53/523 , B01D53/40 , B01D53/68 , B01D2251/2065 , B01D2251/304 , B01D2251/306 , B01D2251/404 , B01D2251/604 , B01D2257/2025 , B01D2257/2045 , B01D2257/302 , B01D2257/304
摘要： Methods and apparatuses are disclosed for the continuous treatment of gas streams contaminated with one or more acid gases, for example HCI, H2S, SO2, SO3, and/or Cl2. At least primary and secondary neutralization zones are utilized, with the secondary neutralization zone being fed by a portion of the gas stream that is used to carry out essentially complete neutralization of a neutralization solution, such as aqueous sodium hydroxide, prior to its disposal (e.g., via biological treatment). The flow of this portion of the gas stream may be regulated by periodically or continuously monitoring the concentration or pH of the spent neutralization solution exiting the secondary neutralization zone. Suitable gas streams that can be treated include effluent gases comprising hydrogen chloride from hydrocarbon conversion processes, particularly paraffin isomerization processes, utilizing a chloriding agent as a catalyst promoter.
摘要翻译：公开了用于连续处理被一种或多种酸性气体例如HCl，H2S，SO2，SO3和/或Cl2污染的气流的方法和装置。至少使用一级和二级中和区，二级中和区由一部分气流进料，该气流用于在其处置之前进行基本上完全中和的中和溶液如氢氧化钠水溶液（例如，通过生物处理）。可以通过周期地或连续地监测离开二次中和区的废中和溶液的浓度或pH来调节气流的这一部分的流动。可以处理的合适的气流包括来自烃转化方法的包含氯化氢的废气，特别是使用氯化剂作为催化剂促进剂的链烷烃异构化方法。

10. 发明申请

WO2010147819A2 APPARATUS AND PROCESS FOR ISOMERIZING A HYDROCARBON STREAM 审中-公开
标题翻译：装置和方法用于同化烃流
公开(公告)号：WO2010147819A2
公开(公告)日：2010-12-23
申请号：PCT/US2010037932
申请日：2010-06-09
申请人： UOP LLC , SHECTERLE DAVID J , GARNEY BRYAN S , DAGUIO JOCELYN C , SHAWLEY JAMES M
发明人： SHECTERLE DAVID J , GARNEY BRYAN S , DAGUIO JOCELYN C , SHAWLEY JAMES M
IPC分类号： C07C5/22 , C07B37/08 , C07C7/04 , C10G35/06
CPC分类号： C10G45/58
摘要： One exemplary embodiment can be an apparatus for isomerizing a hydrocarbon stream rich in a C4 hydrocarbon and/or at least one of a C5 and C6 hydrocarbon. The apparatus can include: a first drier and a second drier adapted to receive a fluid including at least one reactant; and a reaction zone communicating with the first drier to receive the fluid including at least one reactant and with the second drier to receive the regenerant. Generally, the first drier operates at a first condition to dry the fluid including at least one reactant and the second drier operates at a second condition during regeneration with a regenerant. The regenerant can pass through a fluid tapering device for regulating the flow of the regenerant to the reaction zone.
摘要翻译：一个示例性实施方案可以是用于异构化富含C 4烃和/或C 5和C 6烃中的至少一种的烃流的装置。该装置可以包括：第一干燥器和第二干燥器，其适于接收包含至少一种反应物的流体; 以及与第一干燥器连通以接收包含至少一种反应物的流体并与第二干燥器接收再生剂的反应区。通常，第一干燥器在第一条件下操作以干燥包含至少一种反应物的流体，并且第二干燥器在用再生剂再生期间在第二条件下操作。再生剂可以通过流体锥形装置，用于调节再生剂流向反应区的流动。

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