公开(公告)号：US10702798B2

公开(公告)日：2020-07-07

申请号：US14921156

申请日：2015-10-23

Applicant: UOP LLC

Inventor： Eric Leeton ,  Gregory J. Schrad ,  David S. Lafyatis ,  Matthew Lippmann ,  Douglas A. Nafis

IPC: B01D15/36 ,  B01D15/08 ,  B01D53/14 ,  B01D21/01 ,  B01D11/04 ,  B01D61/02 ,  B03C5/00 ,  B03C11/00 ,  B03C3/017

Abstract: A process for treating an ionic liquid containing waste stream is described. If there is a liquid waste stream, the liquid waste stream is introduced into a liquid treatment zone. The ionic liquid in the liquid waste stream is neutralized. The concentration of the ionic liquid in the liquid waste stream is determined, and the allowed concentration of the ionic liquid in the liquid waste stream is determined. The concentration of the ionic liquid in the neutralized liquid waste stream is reduced to the allowed concentration, and the liquid waste stream having the allowed concentration is released. If there is a vapor waste stream, the vapor waste stream is introduced into a vapor treatment zone. The vapor waste stream is treated to form a treated vapor waste stream, and the treated vapor waste stream is released to a plant vapor treatment zone.

公开(公告)号：US20180272327A1

公开(公告)日：2018-09-27

申请号：US15994962

申请日：2018-05-31

Applicant: UOP LLC

Inventor： Matthew Lippmann ,  David S. Lafyatis ,  Douglas A. Nafis ,  Kurt Detrick

IPC: B01J31/40 ,  B01J31/02 ,  B01J38/64 ,  C07C7/12 ,  C07C7/13 ,  C07C7/00 ,  C07C7/10 ,  C10G25/02 ,  C10G25/05 ,  C10G53/08 ,  C10G31/00 ,  B01D17/04 ,  B01D17/02 ,  B01D17/06

Abstract: A process removing ionic liquid from a process stream is described. The process stream is introduced into a coalescer to form an ionic liquid stream and a first treated process stream which has less ionic liquid than the process stream. The first treated process stream is introduced into a separator to form a second treated process stream. The second treated process stream has less ionic liquid than the first treated process stream. The separator is selected from a filtration zone comprising sand or carbon, an adsorption zone, a scrubbing zone, an electrostatic separation zone, or combinations thereof.

公开(公告)号：US20170002276A1

公开(公告)日：2017-01-05

申请号：US15196352

申请日：2016-06-29

Applicant: UOP LLC

Inventor： Bryan J. Egolf ,  Pelin Cox ,  Matthew Lippmann

IPC: C10G57/00

CPC classification number: C10G57/00 ,  C10G2400/30

Abstract: The present subject matter relates generally to methods for hydrocarbon conversion. More specifically, the present subject matter relates to methods for integrating reforming and dehydrocyclodimerization, which are both catalytic processes. While dehydrocyclodimerization takes two or more molecules of a light aliphatic hydrocarbon, such as propane or propylene, to form a product aromatic hydrocarbon and hydrogen, platforming takes C6 and higher carbon number reactants, primarily paraffins and naphthenes, to convert to aromatics and hydrogen. This integration enables an opportunity to recombine the light aliphatic hydrocarbon from the platforming process into a more desirable aromatics species.

Abstract translation: 本主题一般涉及烃转化方法。 更具体地，本主题涉及用于整合重整和脱氢环化二聚化的方法，它们都是催化方法。 虽然脱氢环化二聚化需要两个或更多个轻质脂族烃如丙烷或丙烯分子来形成产物芳族烃和氢，但是平台化需要C6和更高碳原子的反应物，主要是链烷烃和环烷烃，以转化成芳烃和氢。 这种整合使得能够将来自平台过程的轻质脂族烃重新组合成更理想的芳族物质。

公开(公告)号：US09527028B2

公开(公告)日：2016-12-27

申请号：US14575563

申请日：2014-12-18

Applicant: UOP LLC

Inventor： Clayton C. Sadler ,  David A. Wegerer ,  Matthew Lippmann

IPC: B01D53/08 ,  B01D53/04

CPC classification number: B01D53/0462 ,  B01D53/0438 ,  B01D53/0454 ,  B01D53/08 ,  B01D2253/104 ,  B01D2253/108 ,  B01D2255/102 ,  B01D2256/16 ,  B01D2256/24 ,  B01D2256/245 ,  B01D2257/2045 ,  B01D2257/2064 ,  B01D2257/2066 ,  B01D2257/80 ,  B01D2259/4009

Abstract: Process for adsorbing a species from a feed gas stream. Feed gas stream is introduced to an adsorption zone having a sorbent. Species from the feed gas stream is adsorbed onto the sorbent at an adsorbing temperature to enrich the sorbent with the species and deplete the species from the feed gas stream. Species-lean product gas stream is output. Species-rich sorbent from the adsorption zone is passed to a regeneration zone. Regenerant gas at a regenerating temperature greater than the adsorbing temperature is introduced into the regeneration zone to strip the species from the species-rich sorbent. Regenerated sorbent from the regeneration zone passes to a cooling zone disposed below the regeneration zone. Regenerated sorbent is cooled at a cooling temperature below the regenerating temperature. Cooled sorbent is transferred to the adsorbent zone.

Abstract translation: 从进料气流中吸附物质的方法。 将进料气流引入具有吸附剂的吸附区。 来自进料气流的物质在吸附温度下吸附到吸附剂上，以使物质富集吸附剂并从进料气流中消耗物质。 输出物种贫产品气流。 来自吸附区的物种丰富的吸附剂被传递到再生区。 在再生温度大于吸附温度的再生气体被引入再生区以从物种丰富的吸附剂中剥离物种。 来自再生区的再生吸附剂传递到设置在再生区下方的冷却区。 再生吸附剂在低于再生温度的冷却温度下冷却。 冷却的吸附剂转移到吸附剂区域。

公开(公告)号：US20160175760A1

公开(公告)日：2016-06-23

申请号：US14575563

申请日：2014-12-18

Applicant: UOP LLC

Inventor： Clayton C. Sadler ,  David A. Wegerer ,  Matthew Lippmann

IPC: B01D53/04

CPC classification number: B01D53/0462 ,  B01D53/0438 ,  B01D53/0454 ,  B01D53/08 ,  B01D2253/104 ,  B01D2253/108 ,  B01D2255/102 ,  B01D2256/16 ,  B01D2256/24 ,  B01D2256/245 ,  B01D2257/2045 ,  B01D2257/2064 ,  B01D2257/2066 ,  B01D2257/80 ,  B01D2259/4009

Abstract: Process for adsorbing a species from a feed gas stream. Feed gas stream is introduced to an adsorption zone having a sorbent. Species from the feed gas stream is adsorbed onto the sorbent at an adsorbing temperature to enrich the sorbent with the species and deplete the species from the feed gas stream. Species-lean product gas stream is output. Species-rich sorbent from the adsorption zone is passed to a regeneration zone. Regenerant gas at a regenerating temperature greater than the adsorbing temperature is introduced into the regeneration zone to strip the species from the species-rich sorbent. Regenerated sorbent from the regeneration zone passes to a cooling zone disposed below the regeneration zone. Regenerated sorbent is cooled at a cooling temperature below the regenerating temperature. Cooled sorbent is transferred to the adsorbent zone.

Abstract translation: 从进料气流中吸附物质的方法。 将进料气流引入具有吸附剂的吸附区。 来自进料气流的物质在吸附温度下吸附到吸附剂上，以使物质富集吸附剂并从进料气流中消耗物质。 输出物种贫产品气流。 来自吸附区的物种丰富的吸附剂被传递到再生区。 在再生温度大于吸附温度的再生气体被引入再生区以从物种丰富的吸附剂中剥离物种。 来自再生区的再生吸附剂传递到设置在再生区下方的冷却区。 再生吸附剂在低于再生温度的冷却温度下冷却。 冷却的吸附剂转移到吸附剂区域。

公开(公告)号：US09302957B2

公开(公告)日：2016-04-05

申请号：US14267742

申请日：2014-05-01

Applicant: UOP LLC

Inventor： Mark P. Lapinski ,  Matthew Lippmann ,  Gregory Funk ,  David James Shecterle ,  Lakshmi P. Mokka

IPC: C07C5/27 ,  C07C7/00 ,  C07C5/00

CPC classification number: C07C7/005 ,  C07C4/06 ,  C07C5/00 ,  C07C5/27 ,  C07C5/2754 ,  C07C6/123 ,  C07C7/04 ,  C07C7/13 ,  C07C2521/04 ,  C07C2523/42 ,  C10G45/62 ,  C10G2300/1044 ,  C10G2300/1081 ,  C07C9/16 ,  C07C9/18 ,  C07C9/08 ,  C07C9/10 ,  C07C9/12 ,  C07C9/14

Abstract: A process for controlling a yield of an isomerization zone. Prior to entering the isomerization zone, C6 cyclic hydrocarbons are removed from a feed stream. Disproportionation reaction selectivity is observed which produces valuable C3 hydrocarbons and C4 hydrocarbons. Also, a higher ring opening conversion of C5 cyclic hydrocarbons is observed. The disproportionation reactions and the ring opening reactions may be selectively controlled by adjusting an amount of C6 cyclic hydrocarbons passed into the isomerization zone.

Abstract translation: 用于控制异构化区的产率的方法。 在进入异构化区之前，从进料流中除去C6环烃。 观察到歧化反应选择性，产生有价值的C3烃和C4烃。 此外，观察到C5环烃的较高的开环转化率。 歧化反应和开环反应可以通过调节进入异构化区的C6环烃的量来选择性地控制。

公开(公告)号：US20150315102A1

公开(公告)日：2015-11-05

申请号：US14267845

申请日：2014-05-01

Applicant: UOP LLC

Inventor： Mark P. Lapinski ,  Matthew Lippmann

IPC: C07C7/00 ,  C07C4/04 ,  C07C5/27

CPC classification number: C07C7/005 ,  C07C4/04 ,  C07C5/27 ,  C07C5/2772 ,  C07C7/04 ,  C07C7/12 ,  C07C2521/06 ,  C10G9/36 ,  C10G45/58 ,  C10G67/06 ,  C10G69/06 ,  C07C9/16 ,  C07C9/15

Abstract: A process for producing a feed for a stream cracker. At least a portion of the C6 cyclic hydrocarbons are removed from a stream prior to it being passed into an isomerization zone. Disproportionation reaction selectivity is increased, producing valuable C3 hydrocarbons and C4 hydrocarbons. Also, a higher ring opening conversion of C5 cyclic hydrocarbons is observed. The yield may be adjusted by controlling an amount of C6 cyclic hydrocarbons passed to the isomerization zone. The catalyst in the isomerization zone is free of chloride, and the streams including effluent from the isomerization zone may be passed to a steam cracker without requiring chloride removal.

Abstract translation: 一种用于生产流裂解器的进料的方法。 至少一部分C 6环状烃在其进入异构化区之前从流中除去。 歧化反应选择性增加，产生有价值的C3烃和C4烃。 此外，观察到C5环烃的较高的开环转化率。 可以通过控制通过异构化区的C6环状烃的量来调节收率。 异构化区域中的催化剂不含氯化物，并且包括来自异构化区域的流出物的流可以被传递到蒸汽裂化器，而不需要除去氯化物。

公开(公告)号：US20150315101A1

公开(公告)日：2015-11-05

申请号：US14267838

申请日：2014-05-01

Applicant: UOP LLC

Inventor： Mark P. Lapinski ,  Matthew Lippmann ,  Gregory Funk

IPC: C07C7/00 ,  C07C5/27

CPC classification number: C07C7/005 ,  C07C5/27 ,  C07C5/2772 ,  C07C7/04 ,  C07C7/12 ,  C07C2521/04 ,  C07C2523/42 ,  C10G35/02 ,  C10G45/58 ,  C07C9/12 ,  C07C9/16 ,  C07C9/15 ,  C07C9/10

Abstract: A process for increasing a yield of an isomerization zone by removing at least a portion of the C6 cyclic hydrocarbons from a stream having iC4 hydrocarbons, iC5 hydrocarbons, and iC6 hydrocarbons prior to the stream being passed into the same isomerization zone. Suppression of the iC4 hydrocarbons does not occur, allowing the iC4 hydrocarbons to be isomerized in the same isomerization zone as the iC5 hydrocarbons and iC6 hydrocarbons.

Abstract translation: 在物流进入相同的异构化区之前，通过从具有iC4烃，iC5烃和iC6烃的物流中除去至少一部分C 6环烃来提高异构化区的产率的方法。 不会发生iC4烃的抑制，允许iC4烃在与iC5烃和iC6烃相同的异构化区域异构化。

公开(公告)号：US20150251971A1

公开(公告)日：2015-09-10

申请号：US14718877

申请日：2015-05-21

Applicant: UOP LLC

Inventor： Stanley J. Frey ,  Paul T. Barger ,  Maureen L. Bricker ,  John Q. Chen ,  Peter K. Coughlin ,  James A. Johnson ,  Joseph A. Kocal ,  Matthew Lippmann ,  Vasant P. Thakkar ,  Kurt M. Vanden Bussche

IPC: C07C4/18 ,  C10B53/00 ,  C10G65/12

CPC classification number: C07C4/18 ,  C07C4/06 ,  C07C7/12 ,  C07C2521/12 ,  C07C2529/06 ,  C07C2529/18 ,  C10B53/00 ,  C10C1/205 ,  C10G1/002 ,  C10G1/02 ,  C10G45/08 ,  C10G45/10 ,  C10G45/12 ,  C10G45/50 ,  C10G45/52 ,  C10G45/54 ,  C10G47/04 ,  C10G47/16 ,  C10G47/18 ,  C10G47/20 ,  C10G65/12 ,  C10G2300/1096 ,  C10G2400/30 ,  C07C15/06

Abstract: A process for selectively dealkylating aromatic compounds includes providing a coal tar stream comprising aromatic compounds and hydrotreating the coal tar stream to reduce a concentration of one or more of organic sulfur, nitrogen, and oxygen in the coal tar stream, and to hydrogenate at least a portion of the aromatic compounds in the coal tar stream. The process further includes hydrocracking the hydrotreated coal tar stream to further hydrogenate the aromatic compounds and to crack at least one ring of multi-ring aromatic compounds to form single-ring aromatic compounds. The single-ring aromatic compounds present in the hydrocracked stream are then dealkylated to remove alkyl groups containing two or more carbon atoms.

Abstract translation: 选择性地使烷基化芳族化合物的方法包括提供包含芳族化合物的煤焦油流并加氢处理煤焦油流以降低煤焦油流中的一种或多种有机硫，氮和氧的浓度，并将至少一种 煤焦油流中芳族化合物的一部分。 该方法还包括加氢裂化加氢处理的煤焦油流，以进一步氢化芳族化合物并裂解至少一个多环芳族化合物环以形成单环芳族化合物。 然后将存在于加氢裂化物流中的单环芳族化合物脱烷基化以除去含有两个或更多个碳原子的烷基。

公开(公告)号：US09073805B2

公开(公告)日：2015-07-07

申请号：US14472096

申请日：2014-08-28

Applicant: UOP LLC

Inventor： Stanley J. Frey ,  Paul T. Barger ,  Maureen L. Bricker ,  John Q. Chen ,  Peter K. Coughlin ,  James A. Johnson ,  Joseph A. Kocal ,  Matthew Lippmann ,  Vasant P. Thakkar ,  Kurt M. Vanden Bussche

IPC: C07C6/12 ,  C07C5/367 ,  C10G47/00 ,  C10G45/00 ,  C07C6/06 ,  C07C4/06 ,  C07C5/10 ,  C10G1/00 ,  C07C7/12

CPC classification number: C10G65/12 ,  C07C4/04 ,  C07C5/367 ,  C07C6/06 ,  C07C6/126 ,  C07C2521/04 ,  C07C2523/42 ,  C07C2523/62 ,  C07C2523/656 ,  C07C2527/126 ,  C10G1/002 ,  C10G69/06 ,  C10G69/08 ,  C10G69/123 ,  C10G2300/1096 ,  C10G2400/30 ,  C07C15/08 ,  C07C15/04 ,  C07C15/06

Abstract: A process for transalkylating a coal tar stream is described. A coal tar stream is provided, and is fractionated to provide at least one hydrocarbon stream having polycyclic aromatics. The hydrocarbon stream is hydrotreated in a hydrotreating zone, and then hydrocracked in a hydrocracking zone. A light aromatics stream is added to the hydrocracking zone. The light aromatics stream comprises one or more light aromatics having a ratio of methyl/aromatic available position that is lower than a ratio of methyl/aromatic available position for the hydrotreated stream. The hydrocracked stream is transalkylated in the hydrocracking zone.