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公开(公告)号:US20230302425A1
公开(公告)日:2023-09-28
申请号:US18004027
申请日:2021-07-06
Applicant: SABIC Global Technologies B.V.
Inventor: Sreekanth Pannala , Arno Johannes Maria Oprins , Lei Chen
CPC classification number: B01J19/2405 , B01J19/246 , B01J4/001 , C10G47/22 , C10G47/32 , C10G2400/20 , C10G2300/1081
Abstract: A reactor and method for the conversion of hydrocarbon gases utilizes a reactor (12, 312, 412, 512, 612) having a unique feed assembly with an original vortex combustion chamber (40, 340, 436, 536, 636), a diverging conduit (48, 348, 448, 548, 648), and a cylindrical reactor chamber (40, 340, 436, 536, 636). This design creates a compact reaction zone and an inwardly swirling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a diverging conduit (48, 348, 448, 548, 648). The feed streams can be introduced into the reactor (12, 312, 412, 512, 612) at any angle (radial, axial, or something between, or a combination of the above forms) with swirling flow components. The feed streams comprise preheated steam and hydrocarbons for cracking. This system provides conditions suitable for efficient cracking of hydrocarbons, such as ethane, to form olefins.
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公开(公告)号:US20230271157A1
公开(公告)日:2023-08-31
申请号:US18313527
申请日:2023-05-08
Applicant: SABIC Global Technologies B.V.
Inventor: Lei Chen , Sreekanth Pannala , David West
CPC classification number: B01J19/245 , B01J4/001 , B01J6/008 , B01J19/2445 , C07C5/327 , B01J2204/002
Abstract: The invention is directed to a chemical reactor (100) having (a) two or more gas reactor elements (12) with each gas reactor element (12) having (i) a first reaction chamber (38), and (ii) a feed assembly unit (36), (b) a second reaction chamber (20) coupled with each of the two or more gas reactor elements (12) and configured to independently receive two or more product streams from the two or more gas reactor elements (12); and optionally, (c) a gas converging section (40) located downstream to the second reaction chamber (20). The invention is further directed to a method of producing chemical products using the chemical reactor (100) of the present invention.
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公开(公告)号:US11826749B2
公开(公告)日:2023-11-28
申请号:US17242610
申请日:2021-04-28
Applicant: SABIC Global Technologies B.V.
Inventor: Sreekanth Pannala , Vladimir Shtern , Lei Chen , David West
IPC: B01J12/00 , B01J19/24 , B01J19/26 , B01J6/00 , B01J4/00 , B01J19/00 , B01J19/02 , C07C2/78 , C07C11/24
CPC classification number: B01J6/008 , B01J4/005 , B01J12/005 , B01J19/0053 , B01J19/02 , B01J19/2405 , B01J19/246 , B01J19/2415 , C07C2/78 , B01J2204/002 , B01J2219/00094 , B01J2219/1943 , C07C11/24
Abstract: A pyrolysis reactor (12) and method for the pyrolysis of hydrocarbon gases (e.g., methane) utilizes a pyrolysis reactor (12) having a unique burner assembly (44) and pyrolysis feed assembly (56) that creates an inwardly spiraling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a burner conduit (46) with a constricted neck portion or nozzle (52). At least a portion of the swirling gas mixture forms a thin, annular mixed gas flow layer immediately adjacent to the burner conduit (46). A portion of the swirling gas mixture is combusted as the swirling gas mixture passes through the burner conduit (46) and a portion of combustion products circulates in the burner assembly (44). This provides conditions suitable for pyrolysis of hydrocarbons or light alkane gas, such as methane or natural gas.
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公开(公告)号:US20240042405A1
公开(公告)日:2024-02-08
申请号:US18490430
申请日:2023-10-19
Applicant: SABIC Global Technologies B.V.
Inventor: Sreekanth Pannala , Vladimir Shtern , Lei Chen , David West
CPC classification number: B01J6/008 , B01J4/005 , B01J12/005 , B01J19/0053 , B01J19/02 , B01J19/2415 , C07C2/78 , B01J19/2405 , B01J19/246 , B01J2204/002 , B01J2219/00094 , B01J2219/1943 , C07C11/24
Abstract: A reactor (12) and method for the conversion of hydrocarbons utilizes a reactor (12) having a unique feed assembly (56) that creates an inwardly spiraling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a conduit (46) with a constricted neck portion or nozzle (52). At least a portion of the swirling gas mixture forms a thin, annular mixed gas flow layer immediately adjacent to the conduit (46). A portion of the swirling gas mixture is combusted as the swirling gas mixture passes through the conduit (46) for conversion of hydrocarbons.
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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:US20210245128A1
公开(公告)日:2021-08-12
申请号:US17242610
申请日:2021-04-28
Applicant: SABIC Global Technologies B.V.
Inventor: Sreekanth Pannala , Vladimir Shtern , Lei Chen , David West
Abstract: A pyrolysis reactor (12) and method for the pyrolysis of hydrocarbon gases (e.g., methane) utilizes a pyrolysis reactor (12) having a unique burner assembly (44) and pyrolysis feed assembly (56) that creates an inwardly spiraling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a burner conduit (46) with a constricted neck portion or nozzle (52). At least a portion of the swirling gas mixture forms a thin, annular mixed gas flow layer immediately adjacent to the burner conduit (46). A portion of the swirling gas mixture is combusted as the swirling gas mixture passes through the burner conduit (46) and a portion of combustion products circulates in the burner assembly (44). This provides conditions suitable for pyrolysis of hydrocarbons or light alkane gas, such as methane or natural gas.
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公开(公告)号:US11020719B2
公开(公告)日:2021-06-01
申请号:US16977644
申请日:2019-03-07
Applicant: SABIC Global Technologies B.V.
Inventor: Sreekanth Pannala , Vladimir Shtern , Lei Chen , David West
Abstract: A pyrolysis reactor (12) and method for the pyrolysis of hydrocarbon gases (e.g., methane) utilizes a pyrolysis reactor (12) having a unique burner assembly (44) and pyrolysis feed assembly (56) that creates an inwardly spiraling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a burner conduit (46) with a constricted neck portion or nozzle (52). At least a portion of the swirling gas mixture forms a thin, annular mixed gas flow layer immediately adjacent to the burner conduit (46). A portion of the swirling gas mixture is combusted as the swirling gas mixture passes through the burner conduit (46) and a portion of combustion products circulates in the burner assembly (44). This provides conditions suitable for pyrolysis of hydrocarbons or light alkane gas, such as methane or natural gas.
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公开(公告)号:US20230256406A1
公开(公告)日:2023-08-17
申请号:US18004020
申请日:2021-07-06
Applicant: SABIC Global Technologies B.V.
Inventor: Lei Chen , Sreekanth Pannala , David West
CPC classification number: B01J4/005 , B01J12/005 , B01J19/2405 , B01J19/243 , B01J19/248 , C10G47/22 , B01J2219/185 , B01J2219/00121 , B01J2204/002 , B01J2204/007
Abstract: A reactor and method for the conversion of hydrocarbon gases utilizes a reactor (12, 312, 412, 512, 612, 712) having a unique feed assembly with an original vortex combustion chamber (40, 340, 436, 536, 636, 736), a diverging conduit (48, 348, 448, 548, 648, 748), and a cylindrical reactor chamber (40, 340, 436, 536, 636, 736). This design creates a compact combustion zone and an inwardly swirling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a diverging conduit (48, 348, 448, 548, 648, 748). The feed streams can be introduced into the reactor at any angle (perpendicular, axial, or something between, or a combination of the above forms) with swirling flow components. This provides conditions suitable for efficient cracking of hydrocarbons, such as ethane, to form olefins.
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公开(公告)号:US20210046440A1
公开(公告)日:2021-02-18
申请号:US16977644
申请日:2019-03-07
Applicant: SABIC Global Technologies B.V.
Inventor: Sreekanth Pannala , Vladimir Shtern , Lei Chen , David West
Abstract: A pyrolysis reactor (12) and method for the pyrolysis of hydrocarbon gases (e.g., methane) utilizes a pyrolysis reactor (12) having a unique burner assembly (44) and pyrolysis feed assembly (56) that creates an inwardly spiraling fluid flow pattern of the feed gases to form a swirling gas mixture that passes through a burner conduit (46) with a constricted neck portion or nozzle (52). At least a portion of the swirling gas mixture forms a thin, annular mixed gas flow layer immediately adjacent to the burner conduit (46). A portion of the swirling gas mixture is combusted as the swirling gas mixture passes through the burner conduit (46) and a portion of combustion products circulates in the burner assembly (44). This provides conditions suitable for pyrolysis of hydrocarbons or light alkane gas, such as methane or natural gas.
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