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1. 发明授权

US08163067B2 Apparatus and process for isomerizing a hydrogen stream 有权
标题翻译：氢流异构化的装置和方法
公开(公告)号：US08163067B2
公开(公告)日：2012-04-24
申请号：US12485233
申请日：2009-06-16
申请人： Bryan S. Garney , Jocelyn C. Daguio , Kurt A. Detrick , Douglas A. Becci , David J. Shecterle , John M. Krupczak , Andrew D. Mezera
发明人： Bryan S. Garney , Jocelyn C. Daguio , Kurt A. Detrick , Douglas A. Becci , David J. Shecterle , John M. Krupczak , Andrew D. Mezera
IPC分类号： C10G35/02
CPC分类号： C10G45/58 , C10G35/00
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 is displaced from the drier using a down-flow regenerant displacement assembly.
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括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。再生剂使用下流再生剂置换组件从干燥器中移出。

2. 发明申请

US20100314293A1 Apparatus and Process for Isomerizing a Hydrocarbon Stream 有权
标题翻译：用于异构化烃流的装置和方法
公开(公告)号：US20100314293A1
公开(公告)日：2010-12-16
申请号：US12485259
申请日：2009-06-16
申请人： David J. Shecterle , Bryan S. Garney , James M. Shawley , Jocelyn C. Daguio
发明人： David J. Shecterle , Bryan S. Garney , James M. Shawley , Jocelyn C. Daguio
IPC分类号： C10G33/00 , B01J8/00
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：容纳包含至少一种反应物的流体的容器; 流体输送装置，其接收来自所述容器的至少一种反应物的流体; 至少一个干燥器，接收来自流体输送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流体包括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，用于至少一个调节流动并将再生剂的压力降低到容器。

3. 发明授权

US08163068B2 Apparatus and process for isomerizing a hydrocarbon stream 有权
标题翻译：烃流异构化的装置和方法
公开(公告)号：US08163068B2
公开(公告)日：2012-04-24
申请号：US12485246
申请日：2009-06-16
申请人： David J. Shecterle , Bryan S. Garney , Jocelyn C. Daguio , James M. Shawley
发明人： David J. Shecterle , Bryan S. Garney , Jocelyn C. Daguio , James M. Shawley
IPC分类号： C10G35/02
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括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。

4. 发明授权

US08685175B2 Apparatus and process for isomerizing a hydrocarbon stream 有权
标题翻译：烃流异构化的装置和方法
公开(公告)号：US08685175B2
公开(公告)日：2014-04-01
申请号：US12620147
申请日：2009-11-17
申请人： Bryan S. Garney , Jocelyn C. Daguio , Kurt A. Detrick , David J. Shecterle , John M. Krupczak , Andrew D. Mezera , Douglas A. Becci
发明人： Bryan S. Garney , Jocelyn C. Daguio , Kurt A. Detrick , David J. Shecterle , John M. Krupczak , Andrew D. Mezera , Douglas A. Becci
IPC分类号： B08B7/04 , B01J8/00
CPC分类号： C10G25/12 , C10G45/58
摘要： An apparatus and process for isomerizing a hydrocarbon stream rich in a C4 hydrocarbon and/or at least one of a C5 and C6 hydrocarbon which includes a first drier 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：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和方法，其包括第一干燥器和第二干燥器; 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。在再生后残留在第二干燥器中的二次再生剂可以（1）以间歇方式通过排气至火炬组件; （2）以分批的方式通过下降 - 低压 - 低压装置组合; （3）通过交叉管道清洗装置，以使第二干燥器放回操作时反应和分馏区域的混乱最小化; 或（1）（2）和/或（3）的任何组合，以使第二干燥器放回操作时使反应和分馏区域的混乱最小化。

5. 发明授权

US08313562B2 Apparatus and process for isomerizing a hydrocarbon stream 有权
公开(公告)号：US08313562B2
公开(公告)日：2012-11-20
申请号：US13223694
申请日：2011-09-01
申请人： David J. Shecterle , Bryan S. Garney , Jocelyn C. Daguio , James M. Shawley
发明人： David J. Shecterle , Bryan S. Garney , Jocelyn C. Daguio , James M. Shawley
IPC分类号： C09F9/00
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.

6. 发明申请

US20110309299A1 APPARATUS AND PROCESS FOR ISOMERIZING A HYDROCARBON STREAM 有权
标题翻译：装置和方法用于同化烃流
公开(公告)号：US20110309299A1
公开(公告)日：2011-12-22
申请号：US13223694
申请日：2011-09-01
申请人： David J. Shecterle , Bryan S. Garney , Jocelyn C. Daguio , James M. Shawley
发明人： David J. Shecterle , Bryan S. Garney , Jocelyn C. Daguio , James M. Shawley
IPC分类号： C09F9/00
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括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。

7. 发明申请

US20100316548A1 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：US20100316548A1
公开(公告)日：2010-12-16
申请号：US12482114
申请日：2009-06-10
申请人： Patrick J. Bullen , David J. Shecterle , Jocelyn C. Daguio
发明人： Patrick J. Bullen , David J. Shecterle , Jocelyn C. Daguio
IPC分类号： B01D53/68 , B01D53/40 , B01D53/52 , B01D53/50
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 HCl, 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。至少使用一次和二次中和区，二次中和区由一部分气流进料，该气流用于在其处置之前用于进行基本上完全中和的中和溶液，例如氢氧化钠水溶液（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。

8. 发明申请

US20100314292A1 Apparatus and Process for Isomerizing a Hydrocarbon Stream 有权
标题翻译：用于异构化烃流的装置和方法
公开(公告)号：US20100314292A1
公开(公告)日：2010-12-16
申请号：US12485246
申请日：2009-06-16
申请人： David J. Shecterle , Bryan S. Garney , Jocelyn C. Daguio , James M. Shawley
发明人： David J. Shecterle , Bryan S. Garney , Jocelyn C. Daguio , James M. Shawley
IPC分类号： C10G35/02
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括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。

9. 发明授权

US08062613B2 Apparatus and process for isomerizing a hydrocarbon stream 有权
标题翻译：烃流异构化的装置和方法
公开(公告)号：US08062613B2
公开(公告)日：2011-11-22
申请号：US12620136
申请日：2009-11-17
申请人： Bryan S. Garney , Jocelyn C. Daguio , Kurt A. Detrick , David J. Shecterle , John M. Krupczak , Andrew D. Mezera , Douglas A. Becci
发明人： Bryan S. Garney , Jocelyn C. Daguio , Kurt A. Detrick , David J. Shecterle , John M. Krupczak , Andrew D. Mezera , Douglas A. Becci
IPC分类号： B01J8/00
CPC分类号： C10G45/58 , B01D53/261 , B01J20/18 , B01J20/3408 , B01J20/3458
摘要： An apparatus and process for isomerizing a hydrocarbon stream rich in a C4 hydrocarbon and/or at least one of a C5 and C6 hydrocarbon which includes a first drier 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：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和方法，其包括第一干燥器和第二干燥器; 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。在再生后残留在第二干燥器中的二次再生剂可以（1）以间歇方式通过排气至火炬组件; （2）以分批的方式通过下降 - 低压 - 低压装置组合; （3）通过交叉管道清洗装置，以使第二干燥器放回操作时反应和分馏区域的混乱最小化; 或（1）（2）和/或（3）的任何组合，以使第二干燥器放回操作时使反应和分馏区域的混乱最小化。

10. 发明申请

US20110065567A1 Apparatus and Process for Isomerizing a Hydrocarbon Stream 有权
公开(公告)号：US20110065567A1
公开(公告)日：2011-03-17
申请号：US12620147
申请日：2009-11-17
申请人： Bryan S. Garney , Jocelyn C. Daguio , Kurt A. Detrick , David J. Shecterle , John M. Krupczak , Andrew D. Mezera , Douglas A. Becci
发明人： Bryan S. Garney , Jocelyn C. Daguio , Kurt A. Detrick , David J. Shecterle , John M. Krupczak , Andrew D. Mezera , Douglas A. Becci
IPC分类号： B01J20/34
CPC分类号： C10G25/12 , C10G45/58
摘要： An apparatus and process for isomerizing a hydrocarbon stream rich in a C4 hydrocarbon and/or at least one of a C5 and C6 hydrocarbon which includes a first drier 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.

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