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1. 发明申请

WO2012087690A3 METHODS FOR REMOVING UNSATURATED ALIPHATIC HYDROCARBONS FROM A HYDROCARBON STREAM USING CLAY 审中-公开
公开(公告)号：WO2012087690A3
公开(公告)日：2012-06-28
申请号：PCT/US2011/064774
申请日：2011-12-14
申请人： UOP LLC , JAN, Deng-Yang , SCHULTZ, Michael A. , JOHNSON, James A.
发明人： JAN, Deng-Yang , SCHULTZ, Michael A. , JOHNSON, James A.
IPC分类号： C07C7/12 , C07C7/13 , C07C5/10 , C07B63/04 , B01J20/12
摘要： Disclosed is a method for removing unsaturated aliphatic compounds from a hydrocarbon feed stream by contacting the hydrocarbon feed stream with one of an adsorbent comprising clay, an acidic molecular sieve, and activated carbon to produce a hydrocarbon effluent stream having a lower unsaturated aliphatic content relative to the hydrocarbon feed stream. The hydrocarbon feed stream comprises an aromatic compound, a nitrogen compound, and an unsaturated aliphatic compound.

2. 发明申请

WO2011041258A2 PROCESS FOR REMOVING NITROGEN COMPOUNDS FROM A HYDROCARBON STREAM 审中-公开
标题翻译：从碳氢化合物流中去除氮化合物的方法
公开(公告)号：WO2011041258A2
公开(公告)日：2011-04-07
申请号：PCT/US2010050374
申请日：2010-09-27
申请人： UOP LLC , JAN DENG-YANG , SCHULTZ MICHAEL A , KANAZIREV VLADISLAV I
发明人： JAN DENG-YANG , SCHULTZ MICHAEL A , KANAZIREV VLADISLAV I
IPC分类号： C07C7/13 , C07B63/00 , C10G25/03
CPC分类号： C10G25/05 , C10G2300/1088 , C10G2300/1096 , C10G2300/202
摘要： Disclosed is a process for removing nitrogen from a hydrocarbon feed stream by contacting the hydrocarbon feed stream with an adsorbent at nitrogen removal conditions to produce a hydrocarbon effluent stream having a lower nitrogen content relative to the hydrocarbon feed stream. The hydrocarbon feed stream comprises an aromatic compound, an organic nitrogen compound, and a diolefin compound.
摘要翻译：本发明公开了通过在除氮条件下使烃进料流与吸附剂接触以从烃进料流除去氮以产生相对于烃进料流具有较低氮含量的烃流出物流的方法。烃进料流包含芳族化合物，有机氮化合物和二烯烃化合物。

3. 发明申请

WO2012087690A2 METHODS FOR REMOVING UNSATURATED ALIPHATIC HYDROCARBONS FROM A HYDROCARBON STREAM USING CLAY 审中-公开
标题翻译：使用粘土从油气田移除不饱和脂肪烃的方法
公开(公告)号：WO2012087690A2
公开(公告)日：2012-06-28
申请号：PCT/US2011064774
申请日：2011-12-14
申请人： UOP LLC , JAN DENG-YANG , SCHULTZ MICHAEL A , JOHNSON JAMES A
发明人： JAN DENG-YANG , SCHULTZ MICHAEL A , JOHNSON JAMES A
IPC分类号： C07C7/12 , B01J20/12 , C07B63/04 , C07C5/10 , C07C7/13
CPC分类号： C07B63/04 , B01D15/00 , B01J20/12 , B01J20/18 , B01J20/20 , C07C7/12 , C07C7/13 , C10G25/03 , C07C15/04
摘要： Disclosed is a method for removing unsaturated aliphatic compounds from a hydrocarbon feed stream by contacting the hydrocarbon feed stream with one of an adsorbent comprising clay, an acidic molecular sieve, and activated carbon to produce a hydrocarbon effluent stream having a lower unsaturated aliphatic content relative to the hydrocarbon feed stream. The hydrocarbon feed stream comprises an aromatic compound, a nitrogen compound, and an unsaturated aliphatic compound.
摘要翻译：公开了一种通过使烃进料流与包含粘土，酸性分子筛和活性炭的吸附剂中的一种接触来从烃进料流中除去不饱和脂肪族化合物的方法，以产生相对于烃进料流。烃进料流包含芳族化合物，氮化合物和不饱和脂族化合物。

4. 发明申请

WO2012074691A2 PROCESS AND APPARATUS FOR RECOVERING CATALYTIC PRODUCT 审中-公开
标题翻译：回收催化产品的方法和装置
公开(公告)号：WO2012074691A2
公开(公告)日：2012-06-07
申请号：PCT/US2011059873
申请日：2011-11-09
申请人： UOP LLC , ULAS ACIKGOZ SAADET , SCHULTZ MICHAEL A , ZHU XIN X
发明人： ULAS ACIKGOZ SAADET , SCHULTZ MICHAEL A , ZHU XIN X
IPC分类号： C10G55/06 , B01D19/00 , C10G11/18 , C10G25/00
CPC分类号： C10G11/18 , B01D3/141 , B01D3/143 , C10G70/041 , C10G70/048 , C10G2400/02
摘要： A process and apparatus is disclosed for recovering product from catalytically converted product streams. An integrated debutanizer column provides an LPG stream, a light naphtha stream and a heavy naphtha stream. The integrated debutanizer column may comprise a dividing wall column. The light naphtha stream may be used as an absorbent for a primary absorber column which provides advantageous operation.
摘要翻译：公开了用于从催化转化的产物流中回收产物的方法和装置。综合的脱丁烷塔提供LPG流，轻石脑油流和重石脑油流。整合的脱丁烷塔可以包括分隔壁塔。轻石脑油流可以用作主吸收塔的吸收剂，其提供有利的操作。

5. 发明申请

WO2011041258A3 PROCESS FOR REMOVING NITROGEN COMPOUNDS FROM A HYDROCARBON STREAM 审中-公开
公开(公告)号：WO2011041258A3
公开(公告)日：2011-04-07
申请号：PCT/US2010/050374
申请日：2010-09-27
申请人： UOP LLC , JAN, Deng-Yang , SCHULTZ, Michael, A. , KANAZIREV, Vladislav, I.
发明人： JAN, Deng-Yang , SCHULTZ, Michael, A. , KANAZIREV, Vladislav, I.
IPC分类号： C07C7/13 , C07B63/00 , C10G25/03
摘要： Disclosed is a process for removing nitrogen from a hydrocarbon feed stream by contacting the hydrocarbon feed stream with an adsorbent at nitrogen removal conditions to produce a hydrocarbon effluent stream having a lower nitrogen content relative to the hydrocarbon feed stream. The hydrocarbon feed stream comprises an aromatic compound, an organic nitrogen compound, and a diolefin compound.

6. 发明申请

WO2008147638A1 PROCESS FOR PRODUCING CUMENE 审中-公开
标题翻译：生产过程的方法
公开(公告)号：WO2008147638A1
公开(公告)日：2008-12-04
申请号：PCT/US2008/062637
申请日：2008-05-05
申请人： UOP LLC , SCHULTZ, Michael A. , LANKTON, Steven P. , TAGAMOLILA, Constante P.
发明人： SCHULTZ, Michael A. , LANKTON, Steven P. , TAGAMOLILA, Constante P.
IPC分类号： C07C15/085 , C07C1/20 , C07D301/19
CPC分类号： C07C15/085 , C07C2/66 , C07C6/126 , C07C37/08 , C07C45/53 , C07C49/08 , C07C39/04
摘要： A process involves contacting, in an alkylation zone (2), a first benzene recycle stream (8) and a propylene feed stream (6) with an alkylation catalyst to form cumene (10). In a transalkylation zone (4), a polyisopropyl benzene recycle stream (42) and a second benzene recycle stream (20) are contacted with a transalkylation catalyst to form additional cumene (12). The effluents are passed into a dividing wall distillation column (14). A cumene stream (32) is removed from an intermediate point of the dividing wall fractionation column; a first benzene recycle stream (18) is removed from a first end and a heavy aromatics stream (34) is removed from a second end. A second benzene recycle stream (20) is removed from an intermediate point located between the first end and the cumene stream. A polyisopropyl benzene stream (42) is removed from an intermediate point of located between the second end and the cumene stream.
摘要翻译：一种方法包括在烷基化区（2）中与烷基化催化剂接触第一苯循环物流（8）和丙烯进料流（6）以形成枯烯（10）。在烷基转移区（4）中，将聚异丙基苯循环物流（42）和第二苯再循环物流（20）与烷基转移催化剂接触以形成额外的枯烯（12）。流出物流入分隔壁蒸馏塔（14）。从分隔壁分馏塔的中间点除去枯烯物流（32）从第一端除去第一苯回收物流（18），并从第二端除去重质芳烃物流（34）。从位于第一端和异丙基苯流之间的中间点除去第二苯回收物流（20）。从位于第二端和异丙苯流之间的中间点除去聚异丙基苯物流（42）。

7. 发明申请

WO2008147634A1 PROCESS FOR PRODUCING CUMENE 审中-公开
标题翻译：生产过程的方法
公开(公告)号：WO2008147634A1
公开(公告)日：2008-12-04
申请号：PCT/US2008/062598
申请日：2008-05-05
申请人： UOP LLC , SCHULTZ, Michael A. , LANKTON, Steven P. , TAGAMOLILA, Constante P.
发明人： SCHULTZ, Michael A. , LANKTON, Steven P. , TAGAMOLILA, Constante P.
IPC分类号： C07C15/085 , C07C1/20
CPC分类号： C07C15/085 , C07C2/66 , C07C6/126
摘要： In an alkylation zone (2), a benzene recycle stream (8) and a propylene feed stream (6) are reacted to convert the propylene and benzene into cumene (10). In a transalkylation zone (4), a polyisopropylbenzene stream (43) and a benzene recycle stream (20) are reacted to convert the polyisopropylbenzene and benzene into cumene (12). The effluents are passed into a dividing wall fractionation column (14). A cumene product stream (32) is removed from an intermediate point of the dividing wall fractionation column. A benzene recycle stream (18) is removed from a first end, and another benzene recycle stream (20) is removed from an intermediate point of the dividing wall fractionation column. A polyisopropylbenzene stream (34) is removed from a second end of the dividing wall fractionation column. The polyisopropylbenzene stream is passed to a polyisopropylbenzene fractionation column (40) to separate the polyisopropylbenzene (42, 43) from a heavy ends stream (44).
摘要翻译：在烷基化区（2）中，使苯再循环流（8）和丙烯进料流（6）反应，将丙烯和苯转化为异丙苯（10）。在烷基转移区（4）中，使聚异丙基苯料流（43）和苯再循环料流（20）反应，将聚异丙基苯和苯转化成异丙苯（12）。流出物流入分隔壁分馏塔（14）。从分隔壁分馏塔的中间点除去枯烯产物流（32）。从第一端除去苯循环物流（18），从分隔壁分馏塔的中间点除去另一苯回收物流（20）。从分隔壁分馏塔的第二端除去聚异丙基苯料流（34）。将聚异丙基苯流输送到聚异丙基苯分馏塔（40）以将聚异丙基苯（42,43）与重馏分物流（44）分离。

8. 发明申请

WO2008082866A1 FLUIDIZED BED REACTOR WITH BACK-MIXING FOR DEHYDROGENATION OF LIGHT PARAFFINS 审中-公开
标题翻译：具有反混合的流化床反应器，用于脱色轻木素
公开(公告)号：WO2008082866A1
公开(公告)日：2008-07-10
申请号：PCT/US2007/087065
申请日：2007-12-11
申请人： UOP LLC , GLOVER, Bryan K. , ZARRAGA, Julie A. , SCHULTZ, Michael A.
发明人： GLOVER, Bryan K. , ZARRAGA, Julie A. , SCHULTZ, Michael A.
IPC分类号： B01J8/18
CPC分类号： C07C5/324 , C07C5/325 , C07C2521/04 , C07C2521/08 , C07C2521/16 , C07C2523/26 , C07C2523/28 , C07C2523/30 , C07C2523/36 , C07C2523/42 , C07C2523/44 , C07C2523/745 , C07C2523/75 , C07C2523/755 , Y02P20/584 , C07C11/02
摘要： An improved process and system for the endothermic dehydrogenation of an alkane stream (1) is described. The process and system of the present invention comprise a back-mixed fluidized bed reactor (4). The alkane stream is dehydrogenated in a single reactor stage by contacting the alkane stream with a back-mixed fluidized bed (44) of catalyst. Deactivated catalyst (38) is withdrawn from the back-mixed fluidized reactor and heated to produce hot regenerated catalyst (36). The hot regenerated catalyst is returned to the back-mixed fluidized bed reactor at a rate sufficient to maintain the back-mixed fluidized bed reactor at substantially isothermal conditions.
摘要翻译：描述了用于烷烃流（1）的吸热脱氢的改进方法和系统。本发明的方法和系统包括反混流化床反应器（4）。烷烃流在单个反应器阶段通过使烷烃流与催化剂的反混流化床（44）接触而脱氢。将脱活催化剂（38）从反混合流化反应器中取出并加热以产生热再生催化剂（36）。热再生催化剂以足以将反混流化床反应器保持在基本等温条件的速率返回到反混流化床反应器。

9. 发明申请

WO2008042613A3 ABSORPTION RECOVERY PROCESSING OF LIGHT OLEFINS FREE OF CARBON DIOXIDE 审中-公开
标题翻译：不含二氧化碳的轻质烯烃吸收回收工艺
公开(公告)号：WO2008042613A3
公开(公告)日：2008-06-12
申请号：PCT/US2007079028
申请日：2007-09-20
申请人： UOP LLC , SCHULTZ MICHAEL A , TOWLER GAVIN P , WEGERER DAVID A , BRADY JOHN P , LECHNICK WILLIAM J
发明人： SCHULTZ MICHAEL A , TOWLER GAVIN P , WEGERER DAVID A , BRADY JOHN P , LECHNICK WILLIAM J
IPC分类号： C10G11/00 , C10G11/18
CPC分类号： C07C7/005 , B01D53/1475 , B01D53/77 , B01D2256/24 , B01D2257/504 , C07C7/11 , C10G9/206 , C10G2400/20 , Y02C10/06 , Y02P20/152 , Y02P20/51 , Y02P20/52 , Y02P30/40 , Y02P30/442 , C07C11/06 , C07C11/04
摘要： Processing schemes and arrangements for the amine treatment of high olefin content (e.g., ethylene-rich) carbon dioxide-containing streams such as for the effective separation and removal of carbon dioxide therefrom are provided. Corresponding or associated processing schemes and arrangements for the catalytic cracking of a heavy hydrocarbon feedstock (212) and obtaining light olefins substantially free of carbon dioxide via absorption-based product recovery (236) are also provided.
摘要翻译：提供了用于胺处理高烯烃含量（例如富含乙烯）含二氧化碳的料流的加工方案和设置，例如用于有效分离和除去二氧化碳。还提供了用于重质烃原料（212）的催化裂化和通过基于吸收的产物回收（236）获得基本上不含二氧化碳的轻质烯烃的相应或相关的处理方案和装置。

10. 发明申请

WO2008042613A2 ABSORPTION RECOVERY PROCESSING OF LIGHT OLEFINS FREE OF CARBON DIOXIDE 审中-公开
标题翻译：无氧二氧化碳的轻油的吸收回收处理
公开(公告)号：WO2008042613A2
公开(公告)日：2008-04-10
申请号：PCT/US2007/079028
申请日：2007-09-20
申请人： UOP LLC , SCHULTZ, Michael, A. , TOWLER, Gavin, P. , WEGERER, David, A. , BRADY, John, P. , LECHNICK, William, J.
发明人： SCHULTZ, Michael, A. , TOWLER, Gavin, P. , WEGERER, David, A. , BRADY, John, P. , LECHNICK, William, J.
IPC分类号： C07C4/02
CPC分类号： C07C7/005 , B01D53/1475 , B01D53/77 , B01D2256/24 , B01D2257/504 , C07C7/11 , C10G9/206 , C10G2400/20 , Y02C10/06 , Y02P20/152 , Y02P20/51 , Y02P20/52 , Y02P30/40 , Y02P30/442 , C07C11/06 , C07C11/04
摘要： Processing schemes and arrangements for the amine treatment of high olefin content (e.g., ethylene-rich) carbon dioxide-containing streams such as for the effective separation and removal of carbon dioxide therefrom are provided. Corresponding or associated processing schemes and arrangements for the catalytic cracking of a heavy hydrocarbon feedstock (212) and obtaining light olefins substantially free of carbon dioxide via absorption-based product recovery (236) are also provided.
摘要翻译：提供了用于胺处理高烯烃含量（例如富含乙烯的二氧化碳）流的方法和装置，以便有效分离和除去二氧化碳。还提供了通过基于吸收的产物回收（236）对重烃原料（212）的催化裂化和基本上不含二氧化碳获得的轻质烯烃的相应或相关的处理方案和布置。

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