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公开(公告)号:US20230226522A1
公开(公告)日:2023-07-20
申请号:US17995320
申请日:2021-02-24
Applicant: SABIC Global Technologies B.V.
Inventor: Byeongjin BAEK , Istvan LENGYEL , Katherine BARTON , Neeta KULKARNI , Dustin FICKEL
CPC classification number: B01J21/04 , B01J35/1014 , B01J37/0207 , B01J37/0236 , B01J37/08 , B01J35/1019 , B01J23/6525 , C07C4/10 , B01J2531/64 , B01J2531/827 , C07C2523/652 , C07C2521/04
Abstract: Catalysts for the hydrogenolysis of butane are described. A supported catalyst for hydrogenolysis of butane to ethane can include a support and a catalytic crystalline bimetallic composition that can include a molybdenum-iridium (Mo—Ir) crystalline composition attached to the support. The supported catalyst has a BET specific surface area of at least 100 m2/g, preferably 100 m2/g to 500 m2/g. Method of use and methods of making the catalyst are also described.
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公开(公告)号:US20220033325A1
公开(公告)日:2022-02-03
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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