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公开(公告)号:US10513492B2
公开(公告)日:2019-12-24
申请号:US15997869
申请日:2018-06-05
Applicant: Chevron Phillips Chemical Company LP
Inventor: Reza Khankal , Henry Hwu , Daniel M. Hasenberg , Christina M. Barry , Mitchell D. Refvik , Michael S. Hankinson
IPC: B01J8/02 , C07C319/06 , B01J8/04 , C07C321/04
Abstract: Disclosed herein are systems and processes involving the catalyzed cleavage reaction of dimethyl sulfide to methyl mercaptan. The catalyzed cleavage reaction can be a standalone system or process, or can be integrated with a methyl mercaptan production plant.
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22.
公开(公告)号:US20190203128A1
公开(公告)日:2019-07-04
申请号:US15862266
申请日:2018-01-04
Applicant: Chevron Phillips Chemical Company LP
Inventor: Vincent D. McGahee , Daniel M. Hasenberg
CPC classification number: C10G35/10 , B01J8/0045 , B01J8/067 , C10G59/00 , C10G59/02 , C10G59/06 , C10G2300/1044
Abstract: A naphtha reforming reactor system comprising a first reactor comprising a first inlet and a first outlet, wherein the first reactor is configured to operate as an adiabatic reactor, and wherein the first reactor comprises a first naphtha reforming catalyst; and a second reactor comprising a second inlet and a second outlet, wherein the second inlet is in fluid communication with the first outlet of the first reactor, wherein the second reactor is configured to operate as an isothermal reactor, and wherein the second reactor comprises a plurality of tubes disposed within a reactor furnace, a heat source configured to heat the interior of the reactor furnace; and a second naphtha reforming catalyst disposed within the plurality of tubes, wherein the first naphtha reforming catalyst and the second naphtha reforming catalyst are the same or different.
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公开(公告)号:US10336614B2
公开(公告)日:2019-07-02
申请号:US16029731
申请日:2018-07-09
Applicant: Chevron Phillips Chemical Company LP
Inventor: Daniel M. Hasenberg , Alex Pauwels , Ives Mertens
Abstract: The present invention discloses a hydrogen sulfide reactor vessel with an external heating system that is conductively and removably attached to an exterior portion of the reactor vessel. Also disclosed are processes for producing hydrogen sulfide utilizing the reactor vessel.
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公开(公告)号:US20180319663A1
公开(公告)日:2018-11-08
申请号:US16029731
申请日:2018-07-09
Applicant: Chevron Phillips Chemical Company LP
Inventor: Daniel M. Hasenberg , Alex Pauwels , Ives Mertens
CPC classification number: C01B17/162 , B01J4/002 , B01J4/004 , B01J10/005 , B01J19/0013 , B01J19/24 , B01J19/2465 , B01J19/30 , B01J2219/00081 , B01J2219/00083 , B01J2219/0009 , B01J2219/00092 , B01J2219/00101 , B01J2219/00103 , B01J2219/00135 , B01J2219/00155 , B01J2219/00765 , B01J2219/0286 , B01J2219/182 , B01J2219/185 , B01J2219/24
Abstract: The present invention discloses a hydrogen sulfide reactor vessel with an external heating system that is conductively and removably attached to an exterior portion of the reactor vessel. Also disclosed are processes for producing hydrogen sulfide utilizing the reactor vessel.
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公开(公告)号:US10052602B2
公开(公告)日:2018-08-21
申请号:US15629967
申请日:2017-06-22
Applicant: Chevron Phillips Chemical Company LP
Inventor: Cori A. Demmelmaier-Chang , Daniel M. Hasenberg , Scott H. Brown , Vincent D. McGahee , Scott G. Morrison
CPC classification number: B01J8/009 , B01J8/0214 , B01J8/0278 , B01J8/0285 , B01J8/0403 , B01J8/0419 , B01J8/0492 , B01J8/0496 , B01J2208/00212 , B01J2208/0053 , B01J2208/00893 , B01J2208/027 , C01B3/501 , C07C5/41
Abstract: The present invention discloses aromatization reactor vessels with hydrogen membrane tubes, and associated aromatization reactor vessel systems. Also disclosed are processes for conducting aromatization reactions utilizing these reactor vessels and systems.
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26.
公开(公告)号:US10023666B2
公开(公告)日:2018-07-17
申请号:US15377684
申请日:2016-12-13
Applicant: Chevron Phillips Chemical Company LP
Inventor: Jeff S. Lowell , Daniel M. Hasenberg
IPC: C08F110/02 , C08F2/34 , C08F2/44 , C08F210/16
CPC classification number: C08F10/02 , C08F2400/02 , C08F2410/02 , C08F2410/05 , Y02P20/584 , C08F2/34 , C08F4/025 , C08F4/69 , C08F2/005 , C08F2/01
Abstract: A method of transitioning from a first catalyst to a second catalyst in a gas phase fluidized bed reactor comprising continuously feeding the first catalyst and a recycle stream comprising olefin monomer to the reactor; wherein the monomer contacts the first catalyst in the fluidized bed and polymerizes; wherein the reactor is operating in condensing mode (withdrawing a gaseous stream comprising unreacted monomer from the reactor, cooling the gaseous stream to condense a portion thereof, and contacting the cooled gaseous stream with fresh monomer to form the recycle stream); and wherein a liquid phase of the recycle stream evaporates within the fluidized bed; discontinuing the first catalyst to the reactor while continuing to feed the recycle stream; maintaining the condensing mode in reactor at >3 wt. % liquid phase in recycle stream while no fresh catalyst is introduced to reactor; and introducing the second catalyst to the reactor operating in condensing mode.
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公开(公告)号:US09890042B2
公开(公告)日:2018-02-13
申请号:US14963795
申请日:2015-12-09
Applicant: Chevron Phillips Chemical Company LP
Inventor: Daniel M. Hasenberg
IPC: C01B17/69
CPC classification number: C01B17/69 , B01D53/1481 , B01D2252/2056 , B01D2257/302
Abstract: A system for containing an emission of sulfur trioxide, the system comprising a first pressurized vessel, the first pressurized vessel containing sulfur trioxide, a relief vessel containing a volume of a solvent solution, wherein the solvent solution comprises sulfolane, and a first relief conduit providing a first route of fluid communication between the first pressurized vessel and the relief vessel. A method for containing an emission of sulfur trioxide, the method comprising routing a first relief conduit so as to provide a first route of fluid communication between a first pressurized vessel and a relief vessel, wherein the first pressurized vessel contains sulfur trioxide, wherein the relief vessel contains a volume of a solvent solution, and wherein the solvent solution comprises sulfolane.
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28.
公开(公告)号:US12209063B2
公开(公告)日:2025-01-28
申请号:US18508596
申请日:2023-11-14
Applicant: Chevron Phillips Chemical Company LP
Inventor: Kenneth M. Lassen , Michael S. Matson , Daniel M. Hasenberg , Dave C. Schwierman
IPC: B01J8/02 , C07C319/06 , C07C319/14 , C07C319/28 , B01D3/00 , B01D3/02 , C07D227/04 , C07D263/16 , C07D263/22
Abstract: Processes for removing carbon disulfide from product streams containing a sulfide compound are performed by contacting the product stream with an alkanolamine and converting the carbon disulfide to a higher boiling point product, thereby reducing or eliminating carbon disulfide from the product stream. Subsequent removal of the higher boiling point product via distillation can lead to a purified sulfide stream with high purity.
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29.
公开(公告)号:US20240051918A1
公开(公告)日:2024-02-15
申请号:US17884774
申请日:2022-08-10
Applicant: Chevron Phillips Chemical Company LP
Inventor: Kenneth M. Lassen , Ugochukwu Nwagwu , Daniel M. Hasenberg
IPC: C07C319/20 , B01J23/882 , B01J23/883
CPC classification number: C07C319/20 , B01J23/882 , B01J23/883 , C07C2523/882 , C07C2523/883
Abstract: The present disclosure generally relates to processes to produce a mercaptan and an asymmetrical sulfide utilize stacked bed catalyst systems containing CoMo and NiMo, and these processes demonstrate a synergistic reduction in the amount of ethylene, methyl mercaptan, ethyl mercaptan, and H2S in product mixtures. In aspects, the conversion of limiting reactants in the synthesis of asymmetrical sulfides unexpectedly remain high under increased flow rates through the catalyst bed, and under reduced temperatures and pressures. In further aspects, reactor systems configured for the independent synthesis of mercaptans and asymmetrical sulfides in a single fixed bed catalyst vessel are also disclosed as a simplification of existing reactor systems employing separate reactors for separate mercaptan and sulfide syntheses.
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30.
公开(公告)号:US20230046694A1
公开(公告)日:2023-02-16
申请号:US17948718
申请日:2022-09-20
Applicant: Chevron Phillips Chemical Company LP
Inventor: Vincent D. McGahee , Daniel M. Hasenberg
Abstract: A naphtha reforming reactor system comprising a first reactor comprising a first inlet and a first outlet, wherein the first reactor is configured to operate as an adiabatic reactor, and wherein the first reactor comprises a first naphtha reforming catalyst; and a second reactor comprising a second inlet and a second outlet, wherein the second inlet is in fluid communication with the first outlet of the first reactor, wherein the second reactor is configured to operate as an isothermal reactor, and wherein the second reactor comprises a plurality of tubes disposed within a reactor furnace, a heat source configured to heat the interior of the reactor furnace; and a second naphtha reforming catalyst disposed within the plurality of tubes, wherein the first naphtha reforming catalyst and the second naphtha reforming catalyst are the same or different.
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