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Patent Agency Ranking
1.发明申请公开(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
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.
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2.发明申请PROCESS AND APPARATUS FOR IMPROVING LIGHT OLEFIN YIELD FROM A FLUID CATALYTIC CRACKING PROCESS 审中-公开从流体催化裂化过程中改进轻油脂的工艺和装置公开(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。
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3.发明授权公开(公告)号：US10011778B2
公开(公告)日：2018-07-03
申请号：US14109895
申请日：2013-12-17
Applicant: UOP LLC
Inventor： Charles P. Luebke , Kirk Liu , Zhihao Fei
CPC classification number: C10G11/18 , C10G2300/1077 , C10G2400/20
Abstract: The present invention discloses a process optimizing the yield of 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 separation unit stream and a second separation unit stream, the first separation unit stream comprising Cx paraffins, and the second separation unit stream comprising Cx olefins, wherein the second separation unit stream is passed to a second catalytic reactor and the first separation unit stream is removed from the process.
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4.发明授权Process and apparatus for improving light olefin yield from a fluid catalytic cracking process 有权用于从流化催化裂化过程改进轻烯烃产率的方法和设备公开(公告)号：US09468897B2
公开(公告)日：2016-10-18
申请号：US14578181
申请日：2014-12-19
Applicant: UOP LLC
Inventor： Kirk Liu , Zhihao Fei , Charles P. Luebke
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.
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。
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5.发明申请PROCESS AND APPARATUS FOR IMPROVING PROPYLENE YIELD FROM A FLUID CATALYTIC CRACKING PROCESS 有权从流体催化裂化过程中改善丙烯含量的方法和装置公开(公告)号：US20150166433A1
公开(公告)日：2015-06-18
申请号：US14109895
申请日：2013-12-17
Applicant: UOP LLC
Inventor： Charles P. Luebke , Kirk Liu , Zhihao Fei
IPC: C07C4/06
CPC classification number: C10G11/18 , C10G2300/1077 , C10G2400/20
Abstract: The present invention discloses a process optimizing the yield of 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 separation unit stream and a second separation unit stream, the first separation unit stream comprising Cx paraffins, and the second separation unit stream comprising Cx olefins, wherein the second separation unit stream is passed to a second catalytic reactor and the first separation unit stream is removed from the process.
Abstract translation: 本发明公开了一种优化来自流化催化裂化装置的丙烯产率的方法。 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。 分离单元产生第一分离单元流和第二分离单元流，第一分离单元流包含Cx链烷烃，以及包含C x烯烃的第二分离单元流，其中第二分离单元流通入第二催化反应器，并且 从该过程中移除第一分离单元流。
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