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公开(公告)号:US20240367974A1
公开(公告)日:2024-11-07
申请号:US18653397
申请日:2024-05-02
Applicant: UT-Battelle, LLC
Inventor: Sheng Dai , Zhenzhen Yang , Hao Chen
IPC: C01B21/064 , B01J27/24 , B01J37/08 , C07C5/05
Abstract: A composition comprising a boron nitride hexagonal lattice structure in which boron atoms and nitrogen atoms are present in a B:N molar ratio of 1:4-1:8 or 4:1-8:1, wherein the molar ratio corresponds to vacant site defects within the boron nitride hexagonal lattice structure. Also described are methods for producing the boron nitride composition as well as methods for using the boron nitride composition as a catalyst in a hydrogenation process.
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公开(公告)号:US20240043356A1
公开(公告)日:2024-02-08
申请号:US18371412
申请日:2023-09-21
Applicant: AMYRIS, INC.
Inventor: Nicholas OHLER , Karl FISHER , Jin Ki HONG
IPC: C07C5/05 , C10L1/04 , C10M105/04 , C10M107/14 , C07C5/03 , C10M105/02
CPC classification number: C07C5/05 , C10L1/04 , C10M105/04 , C10M107/14 , C07C5/03 , C10M105/02 , C07C2521/04 , C07C2523/44 , C10M2203/0206 , C10M2203/022 , C10M2203/024 , C10M2205/083 , Y02P20/582 , C07C2523/75 , C10M2203/003
Abstract: Provided herein are olefinic feedstocks derived from conjugated hydrocarbon terpenes (e.g., C10-C30 terpenes), methods for making the same, and methods for their use.
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公开(公告)号:US11691934B2
公开(公告)日:2023-07-04
申请号:US17413566
申请日:2019-10-04
Applicant: HANWHA SOLUTIONS CORPORATION
Inventor: Youngjin Kim , Namjin Jang , Kyuho Song , Wook Jeong
IPC: C07C5/05 , B01F27/81 , B01F23/233 , B01F35/221 , B01F27/112 , B01J8/02 , B01J27/13 , B01J31/02 , B01F101/00
CPC classification number: C07C5/05 , B01F23/2331 , B01F27/112 , B01F27/81 , B01F35/2214 , B01J8/02 , B01J27/13 , B01J31/0207 , B01J31/0267 , B01F23/23314 , B01F2101/2204 , B01J2208/00867 , B01J2231/645 , C07C2531/02 , C07C2531/30
Abstract: A synthesis method and a synthesis device of cyclododecene according to the present invention have a high conversion rate of cyclododecatriene which is a reactant and a high selectivity of cyclododecene which is a required product, and even so, have an effect of significantly decreasing a reaction time. In addition, the method and the device have an excellent conversion rate of cyclododecatriene and an excellent selectivity of cyclododecene, while maintaining excellent reactivity without an organic solvent such as ethanol. Therefore, a volume of the reactor relative to an output of cyclododecene may be further decreased. Moreover, the method and the device may minimize costs for facilities and process, are practical, decrease a process time, and are industrially advantageous for mass production as compared with the conventional art.
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公开(公告)号:US20230091233A1
公开(公告)日:2023-03-23
申请号:US17904682
申请日:2021-03-09
Applicant: ExxonMobil Chemical Patents Inc.
Inventor: Alok Srivastava , Rodney S. Smith , James P. Chapman
Abstract: The present disclosure relates to processes, apparatuses, and systems for the removal of sulfur compounds from a heavy hydrocarbon feed as part of steam cracking processes to produce light olefins. In at least one embodiment, the process includes introducing a hydrocarbon feed having a first sulfur content to a steam cracker to produce a steam cracker effluent having a second sulfur content less than the first sulfur content. The process includes introducing the steam cracker effluent to a fractionation system to produce a light hydrocarbon product stream having a third sulfur content less than the second sulfur content.
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5.
公开(公告)号:US20230045639A1
公开(公告)日:2023-02-09
申请号:US17904764
申请日:2021-03-16
Applicant: KOREA INSTITUTE OF MACHINERY & MATERIALS
Inventor: Dae-hoon LEE , Duy Khoe DINH , Hong Jae KANG , Kwan-Tae KIM , Hohyun SONG , You-Na KIM , Heesoo LEE , Younghoon SONG
Abstract: A method of converting a hydrocarbon-based material into acetylene or ethylene according to an embodiment of the present invention includes a supply step of supplying a gaseous or liquid hydrocarbon-based material to a plasma reactor, and a temperature control step of creating a temperature condition of a decomposition reaction of converting the hydrocarbon-based material into acetylene or ethylene in a reaction space in the plasma reactor.
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公开(公告)号:US11407952B2
公开(公告)日:2022-08-09
申请号:US17045669
申请日:2019-04-18
Applicant: SABIC Global Technologies B.V. , Saudi Arabian Oil Company
Inventor: Guillermo Leal , Mohammed Bismillah Ansari , Kareemuddin Mahaboob Shaik , Hiren Shethna , Zhonglin Zhang
Abstract: A method of producing a fuel additive includes: passing a first process stream comprising C4 hydrocarbons through a methyl tertiary butyl ether synthesis unit producing a first recycle stream; passing the first recycle stream through a hydration unit producing the fuel additive and a second recycle stream; passing the second recycle stream through a recycle hydrogenation unit and a deisobutanizer unit; and recycling the second recycle stream to the methyl tertiary butyl ether synthesis unit.
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公开(公告)号:US11274068B2
公开(公告)日:2022-03-15
申请号:US16936990
申请日:2020-07-23
Applicant: Saudi Arabian Oil Company , JGC Catalysts and Chemicals, Ltd. , Japan Cooperation Center Petroleum
Inventor: Omer Refa Koseoglu , Robert Peter Hodgkins , Mitsunori Watabe , Koji Uchida
IPC: C07C6/04 , B01J29/70 , B01J29/08 , B01J29/80 , B01J35/10 , C07C5/05 , B01J29/04 , B01J29/06 , B01J29/89 , B01J29/00 , B01J37/00 , C07C5/02 , C07C5/03
Abstract: Methods for interconverting olefins in an olefin-rich hydrocarbon stream include contacting the olefin-rich hydrocarbon stream with a catalyst system in an olefin interconversion unit to produce an interconverted effluent comprising ethylene and propylene. The contacting may be conducted at a reaction temperature from 450° C. to 750° C., a reaction pressure from 1 bar to 5 bar, and a residence time from 0.5 seconds to 1000 seconds. The catalyst system includes a framework-substituted beta zeolite. The framework-substituted beta zeolite has a *BEA aluminosilicate framework that has been modified by substituting a portion of framework aluminum atoms of the *BEA aluminosilicate framework with beta-zeolite Al-substitution atoms independently selected from the group consisting of titanium atoms, zirconium atoms, hafnium atoms, and combinations thereof.
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公开(公告)号:US11254627B2
公开(公告)日:2022-02-22
申请号:US17132339
申请日:2020-12-23
Applicant: Lummus Technology LLC
Inventor: Greg Nyce , Peter Czerpak , Carlos Faz , Jarod McCormick , William Michalak , Bipinkumar Patel , Guido Radaelli , Tim A. Rappold , Ron Runnebaum , Erik C. Scher , Aihua Zhang , Joel Cizeron
IPC: C07C1/02 , C07C1/04 , C07C1/06 , C07C1/12 , C07C2/50 , C07C2/84 , B01J29/40 , B01J19/00 , B01J19/24 , C10G9/00 , C10G11/00 , C10G50/00 , C10G57/00 , F25J3/02 , C07C2/12 , C07C5/327 , C07C5/09 , C07C5/05 , C07C4/02 , C10G57/02 , C10L3/10 , C07C2/58
Abstract: Integrated systems are provided for the production of higher hydrocarbon compositions, for example liquid hydrocarbon compositions, from methane using an oxidative coupling of methane system to convert methane to ethylene, followed by conversion of ethylene to selectable higher hydrocarbon products. Integrated systems and processes are provided that process methane through to these higher hydrocarbon products.
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9.
公开(公告)号:US20210301213A1
公开(公告)日:2021-09-30
申请号:US16830759
申请日:2020-03-26
Applicant: Saudi Arabian Oil Company
Inventor: Sohel K Shaikh , Raed H Abudawoud , Zhonglin Zhang , Munir D Khokhar , Furqan Aljumah
Abstract: Processes for producing olefins include integration of steam cracking with a dual catalyst metathesis process. The processes include steam cracking a hydrocarbon feed to form a cracking reaction effluent containing butenes, separating the cracking reaction effluent to produce a cracking C4 effluent including normal butenes, isobutene, and 1,3-butadiene, subjecting the cracking C4 effluent to selective hydrogenation to convert 1,3-butadiene in the cracking C4 effluent to normal butenes, removing isobutene from a hydrogenation effluent to produce a metathesis feed containing normal butenes, and contacting the metathesis feed with a metathesis catalyst and a cracking catalyst directly downstream of the metathesis catalyst to produce a metathesis reaction effluent. Contacting with the metathesis catalyst causes metathesis of normal butenes to produce ethylene, propene, and C5+ olefins, and contacting with the cracking catalyst causes C5+ olefins produced through metathesis to undergo cracking reactions to produce additional propene, ethylene, or both.
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公开(公告)号:US20210214290A1
公开(公告)日:2021-07-15
申请号:US17054906
申请日:2019-05-06
Applicant: SABIC Global Technologies B.V.
Inventor: Mohammed Bismillah Ansari , Guillermo Leal , Vijay Dinkar Bodas , Naif Mohammed Al-Naddah Al-Otaibi
Abstract: A method of producing a fuel additive includes: passing a raffinate stream comprising C4 hydrocarbons through a hydrogenation unit, forming a first process stream; passing the first process stream through an extractive distillation unit, forming a C4 olefin stream; passing the C4 olefin stream through a stripper column, forming a purified C4 olefin stream; and forming the fuel additive by passing the purified C4 olefin stream through a hydration unit.
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