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公开(公告)号:US20180170841A1
公开(公告)日:2018-06-21
申请号:US15848220
申请日:2017-12-20
Applicant: UOP LLC
Inventor: Robert J. Schmidt , Feng Xu , Joseph A. Montalbano , Ling Zhou , Edwin P. Boldingh , Linda S. Cheng , John J. Senetar
CPC classification number: C07C15/08 , B01D3/143 , B01J8/0005 , B01J8/1827 , B01J8/1863 , B01J8/26 , B01J2208/00176 , C07C1/24 , C07C2/864 , C07C2/865 , C07C15/06 , C07C31/04 , C07C41/09 , C07C43/043 , C10G2300/1088 , C10G2300/1096 , C10G2400/30 , Y02P20/584
Abstract: This present disclosure relates to processes and apparatuses for toluene methylation in an aromatics complex for producing paraxylene. More specifically, the present disclosure relates to processes and apparatuses for toluene methylation within an aromatics complex for producing paraxylene wherein an embodiment uses a riser reactor, another embodiment uses a pre-reactor producing dimethyl ether, and another embodiment uses partial regeneration of the catalyst.
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公开(公告)号:US20220203340A1
公开(公告)日:2022-06-30
申请号:US17137576
申请日:2020-12-30
Applicant: UOP LLC
Inventor: Avram M. Buchbinder , Wei Pan , J. W. Adriaan Sachtler , Jeffrey M. Noga , Xi Zhao , Ling Zhou , John A. Karch
IPC: B01J23/62 , B01J23/58 , B01J21/04 , B01J21/12 , B01J21/06 , B01J35/02 , B01J35/10 , B01J35/00 , B01J23/96 , B01J38/30 , B01J8/18 , B01J8/26 , C07C5/48
Abstract: A process is provided for dehydrogenating a paraffinic hydrocarbon comprising sending the paraffinic hydrocarbon to a fluidized bed reactor to be contacted at dehydrogenation reaction conditions with a catalyst composition comprising less than about 0.0999 wt % platinum and about 0.05-2.5 wt % Group I or Group II elements or a mixture thereof. The catalytic composition is prepared without addition of tin, gallium, indium, germanium or lead.
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公开(公告)号:US20180170828A1
公开(公告)日:2018-06-21
申请号:US15848078
申请日:2017-12-20
Applicant: UOP LLC
Inventor: Robert J. Schmidt , Feng Xu , Joseph A. Montalbano , Ling Zhou , Edwin P. Boldingh , Linda S. Cheng , John J. Senetar
CPC classification number: C07C2/66 , B01J8/0025 , B01J8/1827 , B01J8/1863 , B01J8/26 , B01J29/40 , B01J29/90 , B01J35/023 , B01J35/04 , B01J38/02 , B01J2208/00176 , B01J2208/00557 , B01J2208/027 , C07C2/864 , C07C15/08 , C07C2527/14 , C07C2529/40 , C10G57/005 , Y02P20/52 , Y02P20/584
Abstract: This present disclosure relates to processes and apparatuses for toluene methylation in an aromatics complex for producing paraxylene. More specifically, the present disclosure relates to processes and apparatuses for toluene methylation within an aromatics complex for producing paraxylene wherein an embodiment uses a riser reactor, another embodiment uses a pre-reactor producing dimethyl ether, and another embodiment uses partial regeneration of the catalyst.
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公开(公告)号:US20240109821A1
公开(公告)日:2024-04-04
申请号:US18474040
申请日:2023-09-25
Applicant: UOP LLC
Inventor: Xi Zhao , Ling Zhou , Jan De Ren
IPC: C07C4/06
CPC classification number: C07C4/06
Abstract: The process converts ethylene in a dilute ethylene (dry gas) stream that may be derived from an FCC product to propylene. The process includes an oligomerization step to convert ethylene in the dilute ethylene stream to heavier olefins, and a second reaction step to convert the heavier olefins to propylene. The oligomerization catalyst may be an amorphous silica-alumina base with a Group VIII and/or VIB metal. The catalyst is resistant to feed impurities such as hydrogen sulfide, carbon oxides, hydrogen and ammonia. At least 50 wt-% of the ethylene in the dilute ethylene stream can be converted to C4+ olefins and recycled to the FCC for cracking to propylene.
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公开(公告)号:US20240026234A1
公开(公告)日:2024-01-25
申请号:US18225061
申请日:2023-07-21
Applicant: UOP LLC
Inventor: Sakthivelan Maadasamy Durai , Jan De Ren , Ling Zhou , Pelin Cox , Sathit Kulprathipanja
IPC: C10G51/02
CPC classification number: C10G51/026 , C10G2300/708 , C10G2400/20 , C10G2300/201 , C10G2300/703
Abstract: A process for catalytic production of olefins comprises contacting a first hydrocarbon stream and a first stream of fluid catalyst in a first riser to produce a first cracked product stream and a spent catalyst stream. The first cracked product stream is separated in a main column. An overhead stream from the main column is separated into a second hydrocarbon stream. The second hydrocarbon stream is contacted with a second stream of fluid catalyst in a second riser to produce a second cracked product stream and a first stream of cool catalyst. A third hydrocarbon stream is obtained from the overhead stream and/or from the second cracked product stream. The third hydrocarbon stream is contacted with a third stream of fluid catalyst in a third riser to produce a third cracked product stream and a second stream of cool catalyst.
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公开(公告)号:US20180170842A1
公开(公告)日:2018-06-21
申请号:US15848280
申请日:2017-12-20
Applicant: UOP LLC
Inventor: Robert J. Schmidt , Feng Xu , Joseph A. Montalbano , Ling Zhou , Edwin P. Boldingh , Linda S. Cheng , John J. Senetar
CPC classification number: C07C15/08 , B01J29/40 , B01J29/90 , C07C1/24 , C07C2/864 , C07C15/06 , C07C31/04 , C07C43/043 , C10G2300/1088 , C10G2300/1096 , C10G2400/30 , Y02P20/52 , Y02P20/584
Abstract: This present disclosure relates to processes and apparatuses for toluene methylation in an aromatics complex for producing paraxylene. More specifically, the present disclosure relates to processes and apparatuses for toluene methylation within an aromatics complex for producing paraxylene wherein an embodiment uses a riser reactor, another embodiment uses a pre-reactor producing dimethyl ether, and another embodiment uses partial regeneration of the catalyst.
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公开(公告)号:US20240173699A1
公开(公告)日:2024-05-30
申请号:US18457059
申请日:2023-08-28
Applicant: UOP LLC
Abstract: Processes and apparatuses for activating a dehydrogenation catalyst that include gallium on a support. An additive particle comprising platinum is mixed with the catalyst particles, which may be fresh or deactivated catalyst. The mixture is exposed, in an oxygen containing environment, to a temperature between 650° C. and 1,000° C. The additive particles may be fluidized with the catalyst particles and may active the catalyst in a regenerator.
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