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公开(公告)号:US11254628B1
公开(公告)日:2022-02-22
申请号:US16941031
申请日:2020-07-28
Applicant: SABIC Global Technologies B.V.
Inventor: Heng Shou , Byeongjin Baek , Robert R. Broekhuis , Dustin Fickel , Istvan Lengyel , Emiel Van Kimmenade
Abstract: Processes for the hydrogenolysis of butane are described. A process can include (a) introducing a butane feed and hydrogen to a first hydrogenolysis reactor comprising a hydrogenolysis catalyst, and (b) contacting the butane feed and hydrogen with the hydrogenolysis catalyst at conditions sufficient to produce a first hydrogenolysis product stream. The introduction of the butane feed stream and hydrogen to the first hydrogenolysis reactor can be controlled to maintain a hydrogen to butane molar ratio in the reactor inlet of 0.3:1 to 0.8:1.
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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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