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公开(公告)号:US20210308650A1
公开(公告)日:2021-10-07
申请号:US17288179
申请日:2019-10-23
Applicant: SABIC Global Technologies B.V.
Inventor: Sreekanth Pannala , Byeongjin Baek , Lei Chen , Vladimir Shtern , Istvan Lengyel , David West , Krishnan Sankaranarayanan
Abstract: A reactor (12, 128, 198) and method for the conversion of hydrocarbon gases utilizes a reactor (12, 128, 198) having a unique feed assembly (58, 136, 200) with an original vortex disk-like inlet flow spaces (72, 74, 76, 80, 146, 148, 150, 152, 208, 216, 218), a converging-diverging vortex mixing chamber (116), and a cylindrical reactor chamber (40). This design creates a small combustion zone and an inwardly swirling fluid flow pattern of the feed gases that passes through a converging conduit (48) with a constricted neck portion (54). This provides conditions suitable for efficient cracking of hydrocarbons, such as ethane, to form olefins.
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公开(公告)号:US11123705B1
公开(公告)日:2021-09-21
申请号:US17288179
申请日:2019-10-23
Applicant: SABIC Global Technologies B.V.
Inventor: Sreekanth Pannala , Byeongjin Baek , Lei Chen , Vladimir Shtern , Istvan Lengyel , David West , Krishnan Sankaranarayanan
Abstract: A reactor (12, 128, 198) and method for the conversion of hydrocarbon gases utilizes a reactor (12, 128, 198) having a unique feed assembly (58, 136, 200) with an original vortex disk-like inlet flow spaces (72, 74, 76, 80, 146, 148, 150, 152, 208, 216, 218), a converging-diverging vortex mixing chamber (116), and a cylindrical reactor chamber (40). This design creates a small combustion zone and an inwardly swirling fluid flow pattern of the feed gases that passes through a converging conduit (48) with a constricted neck portion (54). This provides conditions suitable for efficient cracking of hydrocarbons, such as ethane, to form olefins.
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公开(公告)号:US20200048164A1
公开(公告)日:2020-02-13
申请号:US16343095
申请日:2017-10-17
Applicant: SABIC Global Technologies B.V.
Inventor: Sagar Sarsani , Wugeng Liang , Dick Nagaki , Krishnan Sankaranarayanan , David West , Aghaddin Mamedov
Abstract: A method of selecting a stable mixed metal oxide catalyst for an oxidative coupling of methane (OCM) reaction is disclosed. The method may include, obtaining a mixed metal oxide material having catalytically active metal oxides for the OCM reaction and identifying the Tammann temperature (TTam) of at least one of the catalytically active metals oxides of the mixed metal oxide material. The method further includes selecting the mixed metal oxide material for use as a catalyst in the OCM reaction if the at least one catalytically active metal oxides present in the mixed metal oxide material has a TTam greater than a predetermined temperature.
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公开(公告)号:US09902665B2
公开(公告)日:2018-02-27
申请号:US15179478
申请日:2016-06-10
Applicant: Sabic Global Technologies, B.V.
Inventor: Dick A. Nagaki , Zhun Zhao , Myat Noe Zin Myint , Istvan Lengyel , Aghaddin Mamedov , C. William Gundlach, IV , Krishnan Sankaranarayanan , Derek Falcone
IPC: C07C2/76 , C07C5/333 , B01J21/08 , B01J23/745
CPC classification number: C07C2/76 , B01J21/08 , B01J23/745 , C07C5/3332 , C07C2521/08 , C07C2523/745 , Y02P20/52 , Y02P20/582 , C07C11/02 , C07C11/04 , C07C15/04 , C07C15/24 , C07C11/24
Abstract: A method for producing C2+ hydrocarbons and H2 comprising (a) introducing to a reactor a reactant mixture comprising methane, (b) heating the reactant mixture to a preheating temperature to yield a heated mixture, (c) generating free radicals in the heated mixture to form a primary effluent mixture comprising free radicals, C2+ hydrocarbons, H2, and unreacted methane, (d) reacting the primary effluent mixture in a secondary reaction zone to form a secondary effluent mixture comprising C2+ hydrocarbons, H2, free radicals, and unreacted methane, at a secondary reaction zone temperature that is greater than the preheating temperature, wherein a free radicals amount in the primary effluent mixture is greater than a free radicals amount in the secondary effluent mixture, (e) cooling the secondary effluent mixture to a quench temperature lower than the secondary reaction zone temperature to yield a product mixture comprising C2+ hydrocarbons and H2, and (f) recovering the product mixture.
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公开(公告)号:US11827857B2
公开(公告)日:2023-11-28
申请号:US17424665
申请日:2020-01-27
Applicant: SABIC Global Technologies B.V.
Inventor: Ravichander Narayanaswamy , Hatem Belfadhel , Girish Koripelly , Alexander Stanislaus , Krishna Kumar Ramamurthy , Krishnan Sankaranarayanan
CPC classification number: C10G67/14 , C10G7/00 , C10G9/36 , C10G21/003 , C10G47/22 , C10G2300/107 , C10G2300/1033 , C10G2300/1077 , C10G2300/206 , C10G2300/4012 , C10G2300/44 , C10G2300/807 , C10G2400/20 , C10G2400/30
Abstract: Systems and methods for producing olefins and/or aromatics are disclosed. Methods disclosed includes thermal hydro-processing of crude oils and/or heavy oils and/or residues, in a thermal hydro-processing unit, to produce intermediate products, which can then be used to make valuable chemicals such as olefins and aromatics.
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公开(公告)号:US11680028B2
公开(公告)日:2023-06-20
申请号:US17422784
申请日:2020-01-16
Applicant: SABIC Global Technologies B.V.
Inventor: Ravichander Narayanaswamy , Hatem Belfadhel , Girish Koripelly , Alexander Stanislaus , Krishna Kumar Ramamurthy , Krishnan Sankaranarayanan
Abstract: Systems and methods for producing olefins and/or aromatics are disclosed. Methods disclosed includes aqua-processing hydro-processing of crude oils and/or heavy oils and/or residue, in an aqua-processing hydro-processing unit, to produce intermediate products, which can then be used to make valuable chemicals such as olefins and aromatics.
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公开(公告)号:US20190127295A1
公开(公告)日:2019-05-02
申请号:US16302699
申请日:2017-05-09
Applicant: SABIC Global Technologies B.V.
Inventor: Sreekanth Pannala , Balamurali Krishna Ramachandran Nair , Pankaj Singh Gautam , Krishnan Sankaranarayanan , David West , Istvan Lengyel , Chunliang Wu
Abstract: Disclosed herein are processes, apparatuses, and systems for producing chemicals. One system may comprise a wall defining a chamber; a plurality of burners configured in an arrangement within the chamber, wherein each of the burners is supplied with a material and facilitates combustion of the material, and wherein the arrangement defines an inner volume disposed radially inwardly relative thereto; and an injector disposed within the inner volume and configured to introduce a feedstock into the chamber, wherein the plurality of burners provide thermal energy to facilitate thermal pyrolysis of the feedstock.
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