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1. 发明申请

WO2013089859A1 HYDROCARBON DEHYDROGENATION WITH INERT DILUENT 审中-公开
标题翻译：具有惰性二氧化碳的烃脱氢
公开(公告)号：WO2013089859A1
公开(公告)日：2013-06-20
申请号：PCT/US2012/055298
申请日：2012-09-14
申请人： UOP LLC , LEONARD, Laura E. , BOZZANO, Andrea G. , TOWLER, Gavin P.
发明人： LEONARD, Laura E. , BOZZANO, Andrea G. , TOWLER, Gavin P.
IPC分类号： C07C5/32 , C07C5/333 , C07C11/02
CPC分类号： C07C5/333 , C07C11/06 , C07C11/08 , C07C11/10 , C07C11/02 , C07C11/12
摘要： A hydrocarbon dehydrogenation process includes providing the hydrocarbon feed to a reactor. The hydrocarbon feed includes at least one hydrocarbon selected from light paraffins, heavy paraffins, or combinations thereof. The process further includes introducing an inert diluent into the feed stream, contacting the feed stream and the inert diluent with a catalyst in the reactor, and flowing an effluent stream out of the reactor.
摘要翻译：烃脱氢方法包括将烃进料提供到反应器。烃原料包括至少一种选自轻链烷烃，重链烷烃或其组合的烃。该方法还包括将惰性稀释剂引入进料流中，使进料流和惰性稀释剂与反应器中的催化剂接触，并将流出物流流出反应器。

2. 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。

3. 发明申请

WO2013052228A1 INTEGRATED CATALYTIC CRACKING GASOLINE AND LIGHT CYCLE OIL HYDROPROCESSING TO MAXIMIZE P-XYLENE PRODUCTION 审中-公开
标题翻译：集成催化裂化汽油和轻质循环油加氢以最大限度地提高对二甲苯生产
公开(公告)号：WO2013052228A1
公开(公告)日：2013-04-11
申请号：PCT/US2012/053878
申请日：2012-09-06
申请人： UOP LLC , HAIZMANN, Robert , LEONARD, Laura E.
发明人： HAIZMANN, Robert , LEONARD, Laura E.
IPC分类号： C10G11/00 , C10G11/18 , C10G51/04 , C10G53/02 , C10G69/04 , C10G69/14 , C10G55/00 , C07C15/08 , C07C4/06 , C07C7/10 , C07C5/32 , C07C5/42
CPC分类号： C10G61/04 , C10G63/00 , C10G63/08 , C10G67/00 , C10G67/0418 , C10G69/00 , C10G69/04 , C10G2400/30
摘要： A process for maximizing p-xylene production begins by producing a naphtha fraction and a light cycle oil fraction from a fluid catalytic cracking zone. The gasoline and light cycle oil fractions are combined and hydrotreated to produce a hydrotreated product. Fractionation of the hydrotreated product in a fractionation zone makes a light ends cut, a naphtha cut, a hydrocracker feed and an unconverted oil fraction. The hydrocracker feed is sent to a hydrocracking zone to make a hydrocracker product, which is then recycled back to the fractionation zone, feeding the hydrocracker product above an outlet for the hydrocracker feed, but below an outlet for the naphtha cut. The naphtha cut goes to a dehydrogenation zone where hydrogen is removed to make aromatics from naphthenes to make a dehydrogenated naphtha. The dehydrogenated naphtha is fed to an aromatics recovery unit to recover p-xylene and other aromatics.
摘要翻译：通过从流化催化裂化区中生产石脑油馏分和轻循环油馏分开始使对二甲苯生产最大化的方法。将汽油和轻循环油馏分合并加氢处理以产生加氢处理的产物。在分馏区中加氢处理的产物的分馏使轻馏分馏分，石脑油馏分，加氢裂化器进料和未转化的油馏分。将加氢裂化器进料送至加氢裂化区以制备加氢裂化产物，然后将其再循环回分馏区，将加氢裂化产物供给加氢裂化器进料出口，但位于石脑油切割出口下方。石脑油切割进入脱氢区，其中除去氢气以从环烷烃制备芳族化合物以制备脱氢石脑油。将脱氢石脑油加入到芳烃回收装置中以回收对二甲苯和其它芳族化合物。

4. 发明申请

WO2010074954A2 METHOD 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：WO2010074954A2
公开(公告)日：2010-07-01
申请号：PCT/US2009/067101
申请日：2009-12-08
申请人： UOP LLC , BRICKER, Maureen L. , LEONARD, Laura E.
发明人： BRICKER, Maureen L. , LEONARD, Laura E.
IPC分类号： C07C29/60 , C07C31/20 , B01J8/04
CPC分类号： B01J8/0496 , B01J8/0453 , B01J2208/00283 , B01J2208/00353 , C07C29/60 , C07C31/205
摘要： A method and apparatus for converting glycerol into propylene glycol by directing a basic glycerol containing feed and a hydrogen containing gas into a reaction zone including a fixed bed of catalyst that is operating at glycerol conversion conditions where the reactor includes and at least one quench zone and directing a quench material into the quench zone.
摘要翻译：通过将含有甘油的碱性进料和含氢气体引入包括在甘油转化条件下操作的催化剂固定床的反应区中，将甘油转化成丙二醇的方法和设备，其中反应器包括和至少一个骤冷区，并将骤冷材料引入骤冷区。

5. 发明申请

WO2008014150A2 HYDROCRACKING PROCESS 审中-公开
标题翻译：加氢裂化工艺
公开(公告)号：WO2008014150A2
公开(公告)日：2008-01-31
申请号：PCT/US2007/073708
申请日：2007-07-17
申请人： UOP LLC , LEONARD, Laura E. , KOKAYEFF, Peter
发明人： LEONARD, Laura E. , KOKAYEFF, Peter
IPC分类号： C10G11/00
CPC分类号： C10G65/12 , C10G2300/1011 , C10G2300/107 , C10G2300/1077 , C10G2300/202 , C10G2300/207 , C10G2300/301 , C10G2300/4006 , C10G2300/4012 , C10G2300/4081 , Y02P30/20
摘要： A catalytic hydrocracking process wherein a liquid phase stream comprising a hydrocarbonaceous feedstock (1), a liquid phase effluent from a hydrocracking zone (16), and hydrogen in a sufficiently low hydrogen concentration to maintain a liquid phase continuous system is fed into a hydrotreating zone (4) to produce a first hydrocarbonaceous stream comprising hydrocarbons having a reduced level of sulfur and nitrogen. The resulting hydrocarbons having a reduced level of sulfur and nitrogen are introduced into a hydrocracking zone (13) with a sufficiently low hydrogen concentration to maintain a liquid phase continuous system to produce a hydrocracking zone effluent (16) which provides lower boiling range hydrocarbons.
摘要翻译：（1），来自加氢裂化区（16）的液相流出物和氢气浓度足够低的氢气以保持液相的催化加氢裂化方法将连续体系加入加氢处理区（4）以产生包含具有降低的硫和氮含量的烃的第一含烃流。将所得具有降低的硫和氮含量的烃引入具有足够低氢浓度的加氢裂化区（13）中以保持液相连续体系以产生提供低沸程烃的加氢裂化区流出物（16） / p>

6. 发明申请

WO2013052232A1 INTEGRATED CATALYTIC CRACKING AND REFORMING PROCESSES TO IMPROVE P-XYLENE PRODUCTION 审中-公开
标题翻译：综合催化裂化和改性方法改善对二甲苯生产
公开(公告)号：WO2013052232A1
公开(公告)日：2013-04-11
申请号：PCT/US2012/054047
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： C10G69/10 , C10G69/14 , C07C15/08 , C07C4/06 , C07C7/10 , C07C5/32
CPC分类号： C10G69/04 , C10G59/00 , C10G61/04 , C10G63/00 , C10G63/08 , C10G67/00 , C10G67/0418 , C10G69/00 , C10G2400/30
摘要： A process for maximizing p-xylene production includes producing a naphtha fraction and a light cycle oil fraction from a fluid catalytic cracking zone. These fractions are combined and hydrotreated. Fractionation of the hydrotreated product makes a hydrocracker feed that is sent to a hydrocracking zone to make a naphtha cut and a hydrocracker product. The hydrocracker product is recycled back to the fractionation zone, and the naphtha cut is dehydrogenated in a dehydrogenation zone to make aromatics. Reforming catalyst from a catalyst regenerator moves downward through the dehydrogenation zone. Straight run naphtha and raffinate from the aromatics unit are introduced to an additional series of reforming zones. The reforming catalyst moves in parallel through the first reforming zone and the dehydrogenation zones, then is combined for entry to the second and subsequent reforming zones prior to regeneration.
摘要翻译：最大化对二甲苯生产的方法包括从流化催化裂化区产生石脑油馏分和轻循环油馏分。将这些级分合并加氢处理。加氢处理产物的分级使得加氢裂化器进料被送入加氢裂化区以制备石脑油馏分和加氢裂化产物。将加氢裂化产物再循环回分馏区，并在脱氢区中脱氢石脑油馏分以制备芳族化合物。催化剂再生器重整催化剂向下移动通过脱氢区。来自芳烃单元的直馏石脑油和萃余液被引入另外的一系列重整区。重整催化剂通过第一重整区和脱氢区平行移动，然后在再生之前组合进入第二和随后的重整区。

7. 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。

8. 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。

9. 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。

10. 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。

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