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公开(公告)号:US10941348B2
公开(公告)日:2021-03-09
申请号:US15573640
申请日:2016-05-12
Applicant: SABIC Global Technologies B.V.
Inventor: Thabet Mohammed Al-Qahtani , Khalid Karim , Mubarik Ali Bashir , Ali Al-Hammad , Labeeb Chaudhary Ahmed , Saud Al-Khudeer , Abdullah Turki Al-Jaloud
Abstract: Disclosed herein is a system and method capable of producing benzene from a product stream.
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公开(公告)号:US20180290953A1
公开(公告)日:2018-10-11
申请号:US15572333
申请日:2016-05-05
Applicant: SABIC Global Technologies B.V.
Inventor: Labeeb Chaudhary Ahmed , Khalid Karim , Ali Al-Hammad
IPC: C07C29/151 , C01B3/36 , B01J4/00 , C07C29/152 , C10G2/00
CPC classification number: C07C29/1516 , B01J4/001 , C01B3/36 , C01B3/386 , C01B2203/025 , C01B2203/0255 , C01B2203/0261 , C01B2203/061 , C01B2203/062 , C01B2203/1241 , C01B2203/1258 , C07C1/0485 , C07C1/24 , C07C29/1518 , C07C29/152 , C10G2/32 , C10G2/34 , C10G3/00 , C10L3/103 , C10L3/105 , C07C31/04 , C07C31/08 , C07C11/04 , C07C11/06 , C07C11/08 , C07C11/107 , C07C9/04 , C07C9/06 , C07C9/08 , C07C9/10 , C07C9/14
Abstract: In accordance with the present invention, disclosed herein is a method comprising the steps for producing lower molecular weight C1-C5 hydrocarbons and alcohols. Also disclosed herein, are systems utilized to produce low molecular weight C1-C5 hydrocarbons and alcohols.
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公开(公告)号:US20170297012A1
公开(公告)日:2017-10-19
申请号:US15513445
申请日:2015-09-18
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor: Talal Khaled Al-Shammari , Abdulkarim Al-Mutairi , Khalid Karim , Asad Ahamad Khan , Jayen Barochia
CPC classification number: B01J37/18 , B01J23/75 , C07C1/0435 , C07C1/0445 , C07C2523/75 , C10G2/332 , C07C9/02 , C07C11/02
Abstract: The present disclosures and inventions relate to methods of reducing and activating a cobalt catalyst by contacting an at least partially oxidized cobalt catalyst with a reducing gas, such as a first, second, and/or third reducing gas, at a temperature from 220 ° C. to 270 ° C. for at least 8 or 50 hours depending on the reducing gas, thereby reducing and activating the cobalt catalyst.
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公开(公告)号:US10745624B2
公开(公告)日:2020-08-18
申请号:US15572282
申请日:2016-05-05
Applicant: SABIC Global Technologies B.V.
Inventor: Labeeb Chaudhary Ahmed , Khalid Karim , Ali Al-Hammad
Abstract: In accordance with the present invention, disclosed herein is a method comprising the steps for producing lower molecular weight hydrocarbons. Also disclosed herein, is a system utilized to produce low molecular weight hydrocarbons.
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5.
公开(公告)号:US10737236B2
公开(公告)日:2020-08-11
申请号:US15777732
申请日:2016-11-18
Applicant: SABIC Global Technologies B.V.
Inventor: Zeeshan Nawaz , Khalid Karim
Abstract: A reactor for efficient control of endothermic and exothermic catalytic reactions, including, for example, Fischer Tropsch reactions. Also disclosed are methods of delivering coolant materials and gasification source materials to the reactor.
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公开(公告)号:US10384993B2
公开(公告)日:2019-08-20
申请号:US15572333
申请日:2016-05-05
Applicant: SABIC Global Technologies B.V.
Inventor: Labeeb Chaudhary Ahmed , Khalid Karim , Ali Al-Hammad
IPC: C07C29/151 , C01B3/36 , C07C1/04 , C01B3/38 , C07C1/24 , C10G2/00 , C10G3/00 , B01J4/00 , C07C29/152 , C10L3/10
Abstract: In accordance with the present invention, disclosed herein is a method comprising the steps for producing lower molecular weight C1-C5 hydrocarbons and alcohols. Also disclosed herein, are systems utilized to produce low molecular weight C1-C5 hydrocarbons and alcohols.
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公开(公告)号:US20180298292A1
公开(公告)日:2018-10-18
申请号:US15763683
申请日:2016-09-28
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor: Thabet Al-Qahtani , Khalid Karim , Mubarik Ali Bashir , Ali Al-Hammad
Abstract: In accordance with the present invention, disclosed herein is a method comprising the steps for separating syngas and methane from C2-C4 hydrocarbons. Also disclosed herein, are systems utilized to separate syngas and methane from C2-C4 hydrocarbons.
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公开(公告)号:US09969667B2
公开(公告)日:2018-05-15
申请号:US15551397
申请日:2016-02-16
Applicant: SABIC Global Technologies B.V.
Inventor: Zeeshan Nawaz , Ali Al-Hammad , Talal Al-Shammari , Shehzada Khurram , Khalid Karim , Mubarik Ali Bashir , Thabet Al-Qahtani , Abdullah Turki Al-Jaloud , Saud Al-Khudeer
CPC classification number: C07C41/06 , B01J2219/00006 , C07C43/046
Abstract: Disclosed herein is a system comprising: a) a Fischer-Tropsch reactor comprising a first inlet and a first outlet; b) an olefin separator comprising a second inlet and a second outlet; c) a deisobutanizer comprising a third inlet and a third outlet; d) an iso-butane to isobutylene reactor comprising a fourth inlet and a fourth outlet; and e) a MTBE reactor comprising a fifth inlet, the recited structures are in fluid communication.
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公开(公告)号:US20170333862A1
公开(公告)日:2017-11-23
申请号:US15525162
申请日:2015-11-12
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
Inventor: Talal Khaled Al-Shammari , Khalid Karim
CPC classification number: B01J8/067 , B01J8/065 , B01J19/1856 , B01J2208/0053 , B01J2208/025 , B01J2208/065 , C10G2/32 , C10G2/341
Abstract: The present disclosures and inventions relate reactor and method useful in Fischer-Tropsch processes, such as a reactor comprising a first one or more catalyst holding zones, wherein each of the first one or more catalyst holding zones have a first inner surface, wherein the first inner surface defines a first interior space, wherein each of the first one or more catalyst holding zones have a first longitudinal axis, wherein each of the first one or more catalyst holding zones have a first end and a second end, wherein the first inner surface is tapered towards the first longitudinal axis from the first end towards the second end, and wherein each of the first one or more catalyst holding zones are configured to perform an exothermic reaction.
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公开(公告)号:US20170304793A1
公开(公告)日:2017-10-26
申请号:US15521354
申请日:2015-10-29
Applicant: SABIC Global Technologies B.V.
Inventor: Zeeshan Nawaz , Mubarik Ali Bashir , Khalid Karim
IPC: B01J8/02
Abstract: A reactor for hydrocarbon production that separates wax reaction products from lightweight gaseous reaction products. The reactor has a housing, a catalyst bed, a product recovery zone, and a stripping zone. The catalyst bed can be provided in multi-tubular and other fixed bed configurations. The stripping zone receives light-weight gas reaction products from the product recovery zone, while a gas outlet of the housing receives non-lightweight gaseous hydrocarbon reaction products from the product recovery zone. A wax outlet of the housing receives wax products from the product recovery zone.
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