公开(公告)号：US20180318821A1

公开(公告)日：2018-11-08

申请号：US16039091

申请日：2018-07-18

Applicant: UOP LLC

Inventor： Zhihao Fei ,  Lisa M. Wolschlag ,  Brian W. Hedrick

IPC: B01J38/26 ,  B01J38/30 ,  B01J8/28 ,  B01J8/00 ,  C10G11/18

CPC classification number: B01J38/26 ,  B01J8/0025 ,  B01J8/003 ,  B01J8/0055 ,  B01J8/0065 ,  B01J8/008 ,  B01J8/26 ,  B01J8/28 ,  B01J8/34 ,  B01J29/90 ,  B01J38/04 ,  B01J38/30 ,  B01J38/34 ,  B01J2208/00752 ,  B01J2208/00769 ,  B01J2208/00902 ,  B01J2208/00938 ,  B01J2208/00991 ,  C10G11/182 ,  C10G2300/207 ,  C10G2300/708

Abstract: A counter-current catalyst regenerator with at least two stages of counter-current contact is proposed. Each stage may comprise a permeable barrier that allows upward passage of oxygen-containing gas and downward passage of coked catalyst into each stage, but inhibits upward movement of catalyst to mitigate back mixing and approximate true counter-current contact and efficient combustion of coke from catalyst.

公开(公告)号：US20170240821A1

公开(公告)日：2017-08-24

申请号：US15341525

申请日：2016-11-02

Applicant: UOP LLC

Inventor： Zhihao Fei ,  Steven L. Krupa ,  Hosoo Lim ,  Charles P. Luebke ,  Robert Mehlberg ,  Christopher P. Nicholas ,  Lisa M. Wolschlag

IPC: C10G50/00 ,  C10L1/08

CPC classification number: C10G50/00 ,  C10G2300/307 ,  C10G2300/708 ,  C10G2400/04 ,  C10L1/08 ,  C10L2270/026 ,  C10L2290/12

Abstract: Processes for oligomerizing olefins to produce diesel. The oligomerization zone temperature is controlled to counteract catalyst deactivation caused by coking, by contaminants such as cyclo C5 and/or cyclo C6 hydrocarbons, or both. The temperature is increased in increments to ensure that that the oligomerization zone is producing product at a target product yield with a target product quality, which may be measured by a product cetane number. The target product yield is at least 50 wt % and a target product cetane number may be at least 35.

公开(公告)号：US20160176782A1

公开(公告)日：2016-06-23

申请号：US14578167

申请日：2014-12-19

Applicant: UOP LLC

Inventor： Kirk Liu ,  Zhihao Fei ,  Charles P. Luebke

IPC: C07C4/06

CPC classification number: C07C4/06 ,  C07C7/08 ,  C07C2529/035 ,  C07C2529/40 ,  C10G51/026 ,  Y02P20/52 ,  C07C11/04 ,  C07C11/06

Abstract: The present invention discloses a process optimizing the yield of ethylene and propylene from a fluid catalytic cracking unit. The method combines a first catalytic reactor, a fractionation zone, a separation unit and a second catalytic reactor. The separation unit produces a first separate stream comprising C4 olefins and a second separate stream comprising C5 olefins. The separate streams may be combined and are passed to a second catalytic reactor for additional conversion to ethylene and propylene.

Abstract translation: 本发明公开了一种从流化催化裂化装置优化乙烯和丙烯的产率的方法。 该方法结合了第一催化反应器，分馏区，分离单元和第二催化反应器。 分离单元产生包含C4烯烃的第一分离流和包含C5烯烃的第二分离流。 单独的物流可以组合并且被传递到第二催化反应器以进一步转化成乙烯和丙烯。

公开(公告)号：US10239054B2

公开(公告)日：2019-03-26

申请号：US15828186

申请日：2017-11-30

Applicant: UOP LLC

Inventor： Lev Davydov ,  Michael S. Sandacz ,  Paolo Palmas ,  Zhihao Fei ,  Matthew Lippmann

IPC: B01J38/34 ,  B01J8/28 ,  B01J8/18 ,  C10G11/18 ,  B01J38/20 ,  B01J29/90 ,  F23C13/08 ,  B01J38/70 ,  B01J38/02 ,  F27B15/09

Abstract: A counter-current catalyst regenerator with at least two stages of counter-current contact along with a regenerator riser is proposed. Each stage may comprise a permeable barrier that allows upward passage of oxygen-containing gas and downward passage of coked catalyst into each stage, but inhibits upward movement of catalyst to mitigate back mixing and approximate true counter-current contact and efficient combustion of coke from catalyst. The regenerator riser may provide a passage to transport the catalyst and may serve as a secondary stage for coke combustion to provide the regenerated catalyst.

公开(公告)号：US20180265790A1

公开(公告)日：2018-09-20

申请号：US15987865

申请日：2018-05-23

Applicant: UOP LLC

Inventor： Charles P. Luebke ,  Zhihao Fei

IPC: C10G57/02 ,  B01D53/04

CPC classification number: C10G57/02 ,  B01D15/08 ,  B01D53/0423 ,  B01D2253/108 ,  B01D2256/24 ,  B01D2257/40 ,  B01D2259/40092 ,  C07C2/02 ,  C07C2/04 ,  C07C2/06 ,  C07C2/08 ,  C07C2/12 ,  C07C7/12 ,  C07C7/13 ,  C10G25/00 ,  C10G25/003 ,  C10G25/12 ,  C10G50/00 ,  C10G53/04 ,  C10G55/06 ,  C10G2300/1088 ,  C10G2300/202 ,  C10G2400/02 ,  C10G2400/04 ,  C07C11/08 ,  C07C11/10

Abstract: Processes for regenerating adsorbent in a nitrile removal zone. The regenerant comprises a stream of hot liquid that may comprise a portion of the oligomerized effluent or a portion of a hydrotreated effluent. A spent regenerant comprising the desorbed nitriles may be processed along with the oligomerized effluent with existing separation equipment.

公开(公告)号：US20160175798A1

公开(公告)日：2016-06-23

申请号：US14578181

申请日：2014-12-19

Applicant: UOP LLC

Inventor： Kirk Liu ,  Zhihao Fei ,  Charles P. Luebke

IPC: B01J8/24 ,  C07C4/06

CPC classification number: B01J8/26 ,  B01J8/24 ,  B01J2208/00893 ,  C07C4/06 ,  C07C2529/06 ,  C10G11/18 ,  C10G51/026 ,  C10G51/06 ,  C10G55/06 ,  C10G2400/20

Abstract: The present invention discloses a process optimizing the yield of ethylene and propylene from a fluid catalytic cracking unit. The method combines a first catalytic reactor, a fractionation zone, a separation unit and a second catalytic reactor. The separation unit produces a first separate stream comprising C4 olefins and a second separate stream comprising C5 olefins. The separate streams may be combined and are passed to a second catalytic reactor for additional conversion to ethylene and propylene.

公开(公告)号：US20160168049A1

公开(公告)日：2016-06-16

申请号：US14568263

申请日：2014-12-12

Applicant: UOP LLC

Inventor： Michael S. Sandacz ,  Zhihao Fei

IPC: C07C4/06

CPC classification number: C10G11/18 ,  B01J8/003 ,  B01J8/0055 ,  B01J8/006 ,  B01J8/0065 ,  B01J8/1818 ,  B01J8/1836 ,  B01J8/26 ,  B01J29/084 ,  B01J29/40 ,  B01J29/80 ,  B01J29/90 ,  B01J38/28 ,  B01J38/32 ,  B01J2208/0053 ,  B01J2208/00752 ,  B01J2208/00761 ,  B01J2208/0084 ,  B01J2208/00902 ,  B01J2208/00911 ,  B01J2208/00991 ,  C10G2300/70

Abstract: A process and apparatus for heating catalyst is presented. Cooler catalyst is removed from a reactor and heated with a hot gas in a riser, heated in a heating tube or heated in a heating chamber. Heated catalyst is disengaged from the hot gas if necessary and returned to the reactor. The process and apparatus can be used for producing light olefins. The hot gas may be a flue gas from an FCC regenerator or a combustion gas from a heater.

公开(公告)号：US10563135B2

公开(公告)日：2020-02-18

申请号：US15341525

申请日：2016-11-02

Applicant: UOP LLC

Inventor： Zhihao Fei ,  Steven L. Krupa ,  Hosoo Lim ,  Charles P. Luebke ,  Robert Mehlberg ,  Christopher P. Nicholas ,  Lisa M. Wolschlag

IPC: C10G50/00 ,  C10L1/08

Abstract: Processes for oligomerizing olefins to produce diesel. The oligomerization zone temperature is controlled to counteract catalyst deactivation caused by coking, by contaminants such as cyclo C5 and/or cyclo C6 hydrocarbons, or both. The temperature is increased in increments to ensure that that the oligomerization zone is producing product at a target product yield with a target product quality, which may be measured by a product cetane number. The target product yield is at least 50 wt % and a target product cetane number may be at least 35.

公开(公告)号：US09732289B2

公开(公告)日：2017-08-15

申请号：US14317660

申请日：2014-06-27

Applicant: UOP LLC

Inventor： Hosoo Lim ,  Trung Pham ,  Zhihao Fei ,  Grant H. Yokomizo ,  Ping Sun

IPC: C10G69/04 ,  C10G11/18 ,  C10G47/26 ,  C10G69/12 ,  C10G50/00 ,  C10G57/02

CPC classification number: C10G69/04 ,  C10G11/18 ,  C10G47/26 ,  C10G50/00 ,  C10G57/02 ,  C10G69/126 ,  C10G2300/1074 ,  C10G2300/4081 ,  C10G2400/20

Abstract: An integrated process and apparatus for conversion of gas oil and heavy oil is described. The process includes passing a gas oil feed to a fluid catalytic cracking (FCC) zone to obtain a FCC effluent; separating the FCC effluent in a separation zone into at least two fractions comprising a clarified slurry oil fraction and an overhead fraction; passing the clarified slurry oil fraction to a slurry hydrocracking zone forming at least a naphtha stream; and recycling at least a portion of the slurry hydrocracking naphtha stream to the FCC zone.

公开(公告)号：US20160168050A1

公开(公告)日：2016-06-16

申请号：US14568267

申请日：2014-12-12

Applicant: UOP LLC

Inventor： Zhihao Fei ,  Charles P. Luebke ,  Robert L. Mehlberg ,  Hosoo Lim ,  Lisa M. Wolschlag ,  Paolo Palmas

IPC: C07C4/06 ,  B01J8/18 ,  B01J8/00 ,  B01J8/24

CPC classification number: B01J8/0015 ,  B01J8/003 ,  B01J8/0055 ,  B01J8/006 ,  B01J8/0065 ,  B01J8/1818 ,  B01J8/1836 ,  B01J8/26 ,  B01J29/90 ,  B01J38/30 ,  B01J2208/0053 ,  B01J2208/00752 ,  B01J2208/00761 ,  B01J2208/0084 ,  B01J2208/00902 ,  B01J2208/00911 ,  B01J2208/00991 ,  C10G11/18 ,  C10G2300/70

Abstract: A process and apparatus for heating catalyst is presented. Cooler catalyst is removed from a reactor and heated with a hot gas in a riser, heated in a heating tube or heated in a heating chamber. Heated catalyst is disengaged from the hot gas if necessary and returned to the reactor. The process and apparatus can be used for producing light olefins. The hot gas may be a flue gas from an FCC regenerator or a combustion gas from a heater.

Abstract translation: 提出了一种加热催化剂的方法和装置。 将冷却器催化剂从反应器中取出并用提升管中的热气体加热，在加热管中加热或在加热室中加热。 如果需要，加热催化剂与热气脱离，并返回反应器。 该方法和装置可用于生产轻质烯烃。 热气体可以是来自FCC再生器的烟道气或来自加热器的燃烧气体。