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11. 发明申请

WO2012170147A2 PROCESS FOR PRODUCING ONE OR MORE ALKYLATED AROMATICS 审中-公开
标题翻译：生产一种或多种碱性芳族化合物的方法
公开(公告)号：WO2012170147A2
公开(公告)日：2012-12-13
申请号：PCT/US2012/037440
申请日：2012-05-11
申请人： UOP LLC , HAIZMANN, Robert , LEONARD, Laura E. , BOGDAN, Paula L.
发明人： HAIZMANN, Robert , LEONARD, Laura E. , BOGDAN, Paula L.
IPC分类号： C07C2/66 , C07C2/64 , C07C7/04 , C07C15/073
CPC分类号： C07C2/66 , C07C5/13 , C07C5/2791 , C07C5/367 , C07C6/123 , C07C6/126 , C07C7/12 , C07C7/14 , C07C2101/08 , C07C2101/14 , C07C2521/02 , C07C2521/04 , C07C2521/06 , C07C2521/08 , C07C2521/10 , C07C2523/02 , C07C2523/08 , C07C2523/12 , C07C2523/14 , C07C2523/26 , C07C2523/36 , C07C2523/42 , C07C2523/44 , C07C2523/46 , C07C2523/75 , C07C2523/755 , C07C2529/08 , C07C2529/18 , C07C2529/85 , C07C2601/08 , C07C2601/14 , C10G11/18 , C10G29/205 , C10G45/58 , C10G45/64 , C10G57/005 , C10G69/04 , C10G69/123 , C10G2300/4087 , Y02P30/464 , C07C15/08 , C07C13/10 , C07C13/18 , C07C15/04 , C07C15/073
摘要： One exemplary embodiment may be a process for producing one or more alkylated aromatics. Generally, the process includes providing a first stream including an effective amount of benzene for alkylating benzene from a fractionation zone, providing a second stream including an effective amount of ethene for alkylating benzene from a fluid catalytic cracking zone, providing at least a portion of the first and second streams to an alkylation zone; and passing at least a portion of an effluent including ethylbenzene from the alkylation zone downstream of a para -xylene separation zone.
摘要翻译：一个示例性实施方案可以是用于生产一种或多种烷基化芳族化合物的方法。通常，该方法包括提供包含有效量的苯的第一流，用于从分馏区烷基化苯，提供包含有效量的用于从流化催化裂化区烷基化苯的乙烯的第二料流，提供至少一部分第一和第二流到烷基化区; 并使来自包含乙苯的至少一部分流出物从对二甲苯分离区下游的烷基化区通过。

12. 发明申请

WO2010074841A2 METHODS FOR CONVERTING GLYCEROL TO PROPANOL 审中-公开
标题翻译：将甘油转化为丙醇的方法
公开(公告)号：WO2010074841A2
公开(公告)日：2010-07-01
申请号：PCT/US2009/064688
申请日：2009-11-17
申请人： UOP LLC , BRICKER, Maureen L. , LEONARD, Laura E. , KRUSE, Todd M. , VASSILAKIS, James G. , BARE, Simon R.
发明人： BRICKER, Maureen L. , LEONARD, Laura E. , KRUSE, Todd M. , VASSILAKIS, James G. , BARE, Simon R.
IPC分类号： C07C29/128 , C07C31/20 , B01J23/89
CPC分类号： C07C29/60 , C07C29/80 , C07C29/86 , C07C31/205
摘要： A hydrogenolysis method for converting glycerol into propylene glycol by directing a glycerol containing feed having a pH of 10 or more to a reaction section including at least one glycerol conversion catalyst and operating at glycerol conversions conditions to form a reaction product including propylene glycol.
摘要翻译：通过将含有甘油的进料的pH值等于或大于10的甘油引入到包含至少一种甘油转化催化剂的反应区中，并在甘油转化条件下操作以形成甘油转化条件来将甘油转化成丙二醇的氢解方法包括丙二醇的反应产物。

13. 发明申请

WO2009052025A2 HYDROCARBON CONVERSION PROCESS 审中-公开
标题翻译：石油转化过程
公开(公告)号：WO2009052025A2
公开(公告)日：2009-04-23
申请号：PCT/US2008079549
申请日：2008-10-10
申请人： UOP LLC , LEONARD LAURA E , KOKAYEFF PETER , SMITH MICHAEL R
发明人： LEONARD LAURA E , KOKAYEFF PETER , SMITH MICHAEL R
IPC分类号： C07C4/06 , B01J8/00 , C10G11/18
CPC分类号： C10G65/12
摘要： Methods of hydroprocessing hydrocarbon streams are provided that employ substantially liquid-phase hydroprocessing conditions. In one aspect, the method includes directing a hydrocarbonaceous feed stock (12) to a first substantially liquid-phase hydroprocessing zone (20) wherein an effluent (28) from the first substantially liquid-phase hydroprocessing zone (20) is directed to a second substantially liquid-phase hydroprocessing zone (34) generally undiluted with other hydrocarbon streams. In another aspect, the method recycles (14) a liquid portion of a liquid hydrocarbonaceous effluent (50) from the second substantially liquid-phase hydroprocessing zone (34), which preferably includes an amount of hydrogen dissolved therein, to the hydrocarbonaceous feed stock (12) so that the feed (18) to the first substantially liquid-phase hydroprocessing zone (20) has a relatively larger concentration of dissolved hydrogen relative to the hydrocarbonaceous feed stock (12).
摘要翻译：提供加氢处理烃流的方法，其采用基本上液相加氢处理条件。一方面，该方法包括将含烃原料（12）引导到第一基本上液相的加氢处理区（20），其中来自第一基本液相加氢处理区（20）的流出物（28）被引导至第二基本上液相加氢处理区（34）通常用其它烃流未稀释。另一方面，该方法从第二基本上液相加氢处理区（34）再循环（14）液体烃流出物（50）的液体部分，该第二基本液相加氢处理区（34）优选包含一定量的溶解在其中的氢气至烃类原料（ 12），使得到第一基本液相加氢处理区（20）的进料（18）相对于含烃原料（12）具有相对较大的溶解氢浓度。

14. 发明申请

WO2009052017A2 HYDROCRACKING PROCESS 审中-公开
标题翻译：水力过程
公开(公告)号：WO2009052017A2
公开(公告)日：2009-04-23
申请号：PCT/US2008/079445
申请日：2008-10-10
申请人： UOP LLC , KOKAYEFF, Peter , DZIABALA, Bart , LEONARD, Laura E.
发明人： KOKAYEFF, Peter , DZIABALA, Bart , LEONARD, Laura E.
IPC分类号： C10G55/04 , C10G55/06
CPC分类号： C10G65/12 , C10G2300/42
摘要： Methods (10, 110, 210) of hydrocracking hydrocarbon streams (12, 112, 212) are provided that employ substantially liquid-phase continuous hydroprocessing conditions. In one aspect, the method includes a separate hydrotreating and hydrocracking system where the hydrocracking zone (24) is a substantially liquid-phase continuous system. In another aspect, the method includes a two stage hydrocracking system where one or both of the hydrocracking zones (113, 124) (213, 224) are a substantially liquid-phase continuous reaction system.
摘要翻译：提供了加氢裂化烃流（12,112,212）的方法（10,110,210），其采用基本上液相连续的加氢处理条件。一方面，该方法包括单独的加氢处理和加氢裂化系统，其中加氢裂化区（24）是基本上液相连续的系统。另一方面，该方法包括两阶段加氢裂化系统，其中一个或两个加氢裂化区（113,124）（213,224）是基本上液相的连续反应系统。

15. 发明申请

WO2012030601A2 A DESIGN FOR DRYING REGENERATED CATALYST IN ROUTE TO A PROPANE DEHYDROGENATION REACTOR 审中-公开
标题翻译：干法再生催化剂在丙烷脱氢反应器中的设计
公开(公告)号：WO2012030601A2
公开(公告)日：2012-03-08
申请号：PCT/US2011/049038
申请日：2011-08-25
申请人： UOP LLC , MYERS, David N. , PALMAS, Paolo , LEONARD, Laura E. , SPIEKER, Wolfgang A. , MYERS, Vincenza
发明人： MYERS, David N. , PALMAS, Paolo , LEONARD, Laura E. , SPIEKER, Wolfgang A. , MYERS, Vincenza
IPC分类号： B01J8/08 , B01J38/22 , C07C5/333 , C07C11/06
CPC分类号： B01J38/30 , B01J8/28 , B01J8/34 , C07C5/3335 , Y02P20/52 , Y02P20/584 , C07C11/06
摘要： An apparatus and process are presented for drying a catalyst in a reactor-regenerator system. The process includes a continuous operating system with catalyst circulating between a reactor and regenerator, and the catalyst is dried before returning the catalyst to the reactor. The process uses air that is split between the drying stage and the combustion stage without adding equipment outside of the regenerator, minimizing energy, capital cost, and space requirements.
摘要翻译：介绍了一种用于在反应器 - 再生器系统中干燥催化剂的装置和方法。该方法包括使催化剂在反应器和再生器之间循环的连续操作系统，并且在将催化剂返回到反应器之前将催化剂干燥。该过程使用干燥阶段和燃烧阶段之间的空气分离，而无需在再生器外部添加设备，从而最大限度地降低能耗，资金成本和空间要求。

16. 发明申请

WO2010074841A3 METHODS FOR CONVERTING GLYCEROL TO PROPANOL 审中-公开
标题翻译：将甘油转化成丙二醇的方法
公开(公告)号：WO2010074841A3
公开(公告)日：2010-08-26
申请号：PCT/US2009064688
申请日：2009-11-17
申请人： UOP LLC , BRICKER MAUREEN L , LEONARD LAURA E , KRUSE TODD M , VASSILAKIS JAMES G , BARE SIMON R
发明人： BRICKER MAUREEN L , LEONARD LAURA E , KRUSE TODD M , VASSILAKIS JAMES G , BARE SIMON R
IPC分类号： C07C29/128 , B01J23/89 , C07C31/20
CPC分类号： C07C29/60 , C07C29/80 , C07C29/86 , C07C31/205
摘要： A hydrogenolysis method for converting glycerol into propylene glycol by directing a glycerol containing feed having a pH of 10 or more to a reaction section including at least one glycerol conversion catalyst and operating at glycerol conversions conditions to form a reaction product including propylene glycol.
摘要翻译：一种氢解方法，用于通过将含有10或更高pH值的甘油的进料引导到包含至少一种甘油转化催化剂的反应部分并在甘油转化条件下操作以形成包含丙二醇的反应产物，从而将甘油转化成丙二醇。

17. 发明申请

WO2013052233A1 REFORMING PROCESS WITH INTEGRATED FLUID CATALYTIC CRACKER GASOLINE AND HYDROPROCESSED CYCLE OIL 审中-公开
标题翻译：一体化流体催化裂化器汽油和氢化循环油的改造工艺
公开(公告)号：WO2013052233A1
公开(公告)日：2013-04-11
申请号：PCT/US2012/054049
申请日：2012-09-07
申请人： UOP LLC , HAIZMANN, Robert , LEONARD, Laura E.
发明人： HAIZMANN, Robert , LEONARD, Laura E.
IPC分类号： C10G69/00 , C10G69/08
CPC分类号： C10G35/085 , C10G11/18 , C10G35/095 , C10G47/00 , C10G59/00 , C10G63/04 , C10G63/08
摘要： A reforming process includes integrating catalytic cracking product naphtha dehydrogenation and naphtha from a hydrocracking zone and feeding them to a dehydrogenation zone. The dehydrogenation zone includes a first portion of reforming catalyst from a catalyst regenerator that moves downward through the dehydrogenation zone. A product stream from the dehydrogenation zone flows to an aromatics unit and is separated into an aromatic-rich extract and a raffinate. Straight run naphtha and the raffinate are introduced to a first reforming zone that includes a second portion of reforming catalyst. The reforming catalyst moves through the first reforming zone then is removed from the bottom of each of the first reforming zone and the dehydrogenation zone and is fed to a second reforming zone. An effluent from the first reforming zone is fed to a plurality of reforming zones. The reforming catalyst moves downward through the multiple reforming zones then to a regenerator.
摘要翻译：重整过程包括将加氢裂化区的催化裂化产物石脑油脱氢和石脑油整合并将其送入脱氢区。脱氢区包括从催化剂再生器向下移动通过脱氢区的第一部分重整催化剂。来自脱氢区的产物流流入芳烃单元并分离成富含芳香的提取物和萃余液。将直馏石脑油和萃余液引入包括重整催化剂的第二部分的第一重整区。重整催化剂移动通过第一重整区，然后从第一重整区和脱氢区的每一个的底部除去并进料到第二重整区。来自第一重整区的流出物被供给到多个重整区。重整催化剂通过多个重整区向下移动到再生器。

18. 发明申请

WO2012154487A2 PROCESS FOR ALKYLATING BENZENE 审中-公开
标题翻译：碱化苯甲酸的方法
公开(公告)号：WO2012154487A2
公开(公告)日：2012-11-15
申请号：PCT/US2012/036275
申请日：2012-05-03
申请人： UOP LLC , LEONARD, Laura, E. , HAIZMANN, Robert
发明人： LEONARD, Laura, E. , HAIZMANN, Robert
IPC分类号： C07C2/64 , C07C15/04 , C07C15/073 , C07C7/00 , B01J19/24
CPC分类号： C07C2/66 , B01J2219/00006 , C07C4/18 , C07C6/123 , C07C6/126 , C07C2523/06 , C07C2523/08 , C07C2523/12 , C07C2523/14 , C07C2523/28 , C07C2523/30 , C07C2523/36 , C07C2523/42 , C07C2523/44 , C07C2523/46 , C07C2523/745 , C07C2523/75 , C07C2523/755 , C07C2529/08 , C07C2529/70 , C07C2529/84 , C07C2529/85 , C07C15/08 , C07C15/04 , C07C15/06
摘要： One exemplary embodiment can be a process for alkylating benzene. The process can include obtaining at least a portion of a stream from a transalkylation zone, combining the at least the portion of the stream from the transalkylation zone with a fuel gas stream, and providing at least a portion of the combined stream to a benzene methylation zone. Typically, the fuel gas stream includes an effective amount of one or more alkanes for alkylating at least partially from a hydrogen purification process tail gas.
摘要翻译：一个示例性实施方案可以是用于烷基化苯的方法。该方法可以包括从烷基转移区获得至少一部分物流，将来自烷基转移区的物流的至少一部分与燃料气流合并，并将组合物流的至少一部分提供给苯甲基化区。通常，燃料气流包括有效量的一种或多种烷烃，用于至少部分地从氢气净化工艺尾气中烷基化。

19. 发明申请

WO2012009110A2 METHOD FOR QUENCHING PARAFFIN DEHYDROGENATION REACTION IN COUNTER-CURRENT REACTOR 审中-公开
标题翻译：在对流反应器中猝灭石蜡脱氢反应的方法
公开(公告)号：WO2012009110A2
公开(公告)日：2012-01-19
申请号：PCT/US2011/041204
申请日：2011-06-21
申请人： UOP LLC , SPIEKER, Wolfgang, A. , LEONARD, Laura, E. , MYERS, David, N.
发明人： SPIEKER, Wolfgang, A. , LEONARD, Laura, E. , MYERS, David, N.
IPC分类号： B01J8/18 , C07C5/333 , C07C11/06 , C10G11/18
CPC分类号： C07C5/333 , Y10S585/903 , Y10S585/91 , Y10S585/911 , C07C11/06
摘要： A process is presented for quenching a process stream in a paraffin dehydrogenation process. The process comprises cooling a propane dehydrogenation stream during the hot residence time after the process stream leaves the catalytic bed reactor section. The process includes cooling and compressing the product stream, taking a portion of the product stream and passing the portion of the product stream to the mix with the process stream as it leaves the catalytic bed reactor section.
摘要翻译：提出了一种用于在石蜡脱氢过程中骤冷工艺流的方法。该方法包括在工艺物流离开催化床反应器部分之后的热停留时间期间冷却丙烷脱氢物流。该方法包括冷却和压缩产物流，取出一部分产物流，并在产物流离开催化床反应器部分时将该部分产物流与工艺流一起通入混合物中。

20. 发明申请

WO2011056712A2 APPARATUS AND PROCESS FOR RECOVERING FCC PRODUCT 审中-公开
标题翻译：恢复FCC产品的设备和工艺
公开(公告)号：WO2011056712A2
公开(公告)日：2011-05-12
申请号：PCT/US2010054513
申请日：2010-10-28
申请人： UOP LLC , DA SILVA FERREIRA ALVES JOAO J , ULAS ACIKGOZ SAADET , ZHU XIN X , LEONARD LAURA E
发明人： DA SILVA FERREIRA ALVES JOAO J , ULAS ACIKGOZ SAADET , ZHU XIN X , LEONARD LAURA E
IPC分类号： C10G55/06 , B01J29/06 , C10G11/18 , F25J3/00
CPC分类号： C10G11/18 , B01J29/084 , B01J29/40 , B01J29/90 , B01J38/30 , C10G55/06 , C10G70/06 , C10G2300/1044 , C10G2400/20
摘要： An apparatus and process are disclosed for recovering product from catalytically converted product streams. Gaseous unstabilized naphtha from an overhead receiver from a main fractionation column is compressed in a compressor. Liquid unstabilized naphtha from the overhead receiver and liquid naphtha fraction from the compressor are sent to a naphtha splitter column upstream of a primary absorber. Consequently, less naphtha is circulated in the gas recovery system.
摘要翻译：公开了用于从催化转化的产物流中回收产物的装置和方法。来自主分馏塔的塔顶接收器的气态未稳定石脑油在压缩机中被压缩。来自塔顶储存器的液体不稳定石脑油和来自压缩机的液体石脑油馏分被送到主吸收器上游的石脑油分离塔。因此，较少的石脑油在气体回收系统中循环。

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