公开(公告)号：WO2012154487A3

公开(公告)日：2013-05-10

申请号：PCT/US2012036275

申请日：2012-05-03

Applicant: UOP LLC ,  LEONARD LAURA E ,  HAIZMANN ROBERT

Inventor： LEONARD LAURA E ,  HAIZMANN ROBERT

IPC: C07C2/64 ,  B01J19/24 ,  C07C7/00 ,  C07C15/04 ,  C07C15/073

CPC classification number: 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

Abstract: 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.

Abstract translation: 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。

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

Applicant: UOP LLC ,  HAIZMANN, Robert ,  LEONARD, Laura E.

Inventor： HAIZMANN, Robert ,  LEONARD, Laura E.

IPC: 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 classification number: C10G61/04 ,  C10G63/00 ,  C10G63/08 ,  C10G67/00 ,  C10G67/0418 ,  C10G69/00 ,  C10G69/04 ,  C10G2400/30

Abstract: 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.

Abstract translation: 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。

公开(公告)号：WO2012170147A3

公开(公告)日：2013-01-31

申请号：PCT/US2012037440

申请日：2012-05-11

Applicant: UOP LLC ,  HAIZMANN ROBERT ,  LEONARD LAURA E ,  BOGDAN PAULA L

Inventor： HAIZMANN ROBERT ,  LEONARD LAURA E ,  BOGDAN PAULA L

IPC: C07C2/66 ,  C07C2/64 ,  C07C7/04 ,  C07C15/073

CPC classification number: 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

Abstract: 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.

Abstract translation: 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。

公开(公告)号：WO2012009110A3

公开(公告)日：2012-04-19

申请号：PCT/US2011041204

申请日：2011-06-21

Applicant: UOP LLC ,  SPIEKER WOLFGANG A ,  LEONARD LAURA E ,  MYERS DAVID N

Inventor： SPIEKER WOLFGANG A ,  LEONARD LAURA E ,  MYERS DAVID N

IPC: B01J8/18 ,  C07C5/333 ,  C07C11/06 ,  C10G11/18

CPC classification number: C07C5/333 ,  Y10S585/903 ,  Y10S585/91 ,  Y10S585/911 ,  C07C11/06

Abstract: 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.

Abstract translation: 提出了一种在石蜡脱氢过程中淬灭工艺流的方法。 该方法包括在工艺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流。 该方法包括冷却和压缩产物流，取出产物流的一部分，并且当其离开催化床反应器部分时，使产物流的一部分与工艺物流一起进入混合物。

公开(公告)号：WO2011056712A3

公开(公告)日：2011-05-12

申请号：PCT/US2010/054513

申请日：2010-10-28

Applicant: UOP LLC ,  DA SILVA FERREIRA ALVES, Joao J. ,  ULAS ACIKGOZ, Saadet ,  ZHU, Xin, X. ,  LEONARD, Laura, E.

Inventor： DA SILVA FERREIRA ALVES, Joao J. ,  ULAS ACIKGOZ, Saadet ,  ZHU, Xin, X. ,  LEONARD, Laura, E.

IPC: C10G55/06 ,  C10G11/18 ,  F25J3/00 ,  B01J29/06

Abstract: 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.

公开(公告)号：WO2010074954A3

公开(公告)日：2010-11-04

申请号：PCT/US2009067101

申请日：2009-12-08

Applicant: UOP LLC ,  BRICKER MAUREEN L ,  LEONARD LAURA E

Inventor： BRICKER MAUREEN L ,  LEONARD LAURA E

IPC: C07C29/60 ,  B01J8/04 ,  C07C31/20

CPC classification number: B01J8/0496 ,  B01J8/0453 ,  B01J2208/00283 ,  B01J2208/00353 ,  C07C29/60 ,  C07C31/205

Abstract: 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.

Abstract translation: 一种将甘油转化成丙二醇的方法和装置，该方法和装置通过将含有碱性甘油的进料和含氢气体引入反应区，反应区包括在反应器包含的甘油转化条件下操作的固定催化剂床和至少一个骤冷区， 将淬火材料引入淬火区。

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

Applicant: UOP LLC ,  BRICKER, Maureen L. ,  LEONARD, Laura E.

Inventor： BRICKER, Maureen L. ,  LEONARD, Laura E.

IPC: C07C29/60 ,  C07C31/20 ,  B01J8/04

CPC classification number: B01J8/0496 ,  B01J8/0453 ,  B01J2208/00283 ,  B01J2208/00353 ,  C07C29/60 ,  C07C31/205

Abstract: 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.

Abstract translation: 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。

公开(公告)号：WO2009052004A1

公开(公告)日：2009-04-23

申请号：PCT/US2008/079305

申请日：2008-10-09

Applicant: UOP LLC ,  KOKAYEFF, Peter ,  LEONARD, Laura, E.

Inventor： KOKAYEFF, Peter ,  LEONARD, Laura, E.

IPC: C10G65/12 ,  C10G55/06 ,  C07C5/03

CPC classification number: C10G45/58 ,  C10G2400/04

Abstract: A process (10) is provided for improving the cold flow properties of a hydrocarbon stream (14) employing a substantially liquid-phase continuous hydroisomerization zone (12) where the reaction zone has a substantially constant level of dissolved hydrogen throughout without the addition of additional hydrogen external to the reaction zone.

Abstract translation: 提供了一种方法（10），用于改进使用基本上液相的连续加氢异构化区（12）的烃流（14）的冷流性质，其中反应区具有基本上恒定的溶解氢水平，而不添加额外的 反应区外部的氢。

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

Applicant: UOP LLC ,  LEONARD, Laura E. ,  KOKAYEFF, Peter

Inventor： LEONARD, Laura E. ,  KOKAYEFF, Peter

IPC: C10G11/00

CPC classification number: C10G65/12 ,  C10G2300/1011 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/301 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4081 ,  Y02P30/20

Abstract: 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.

Abstract translation: （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>

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

Applicant: UOP LLC ,  LEONARD, Laura E. ,  BOZZANO, Andrea G. ,  TOWLER, Gavin P.

Inventor： LEONARD, Laura E. ,  BOZZANO, Andrea G. ,  TOWLER, Gavin P.

IPC: C07C5/32 ,  C07C5/333 ,  C07C11/02

CPC classification number: C07C5/333 ,  C07C11/06 ,  C07C11/08 ,  C07C11/10 ,  C07C11/02 ,  C07C11/12

Abstract: 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.

Abstract translation: 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。