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公开(公告)号:US11931725B2
公开(公告)日:2024-03-19
申请号:US17867950
申请日:2022-07-19
Applicant: Scientific Design Company, Inc.
Inventor: Xiankuan Zhang , Christelle Verrier
CPC classification number: B01J23/50 , B01J21/04 , B01J23/36 , B01J35/006 , B01J35/08 , C07D301/03 , B82Y30/00 , B82Y40/00
Abstract: A conditioning process that is employed with a high selectivity catalyst (HSC) during an initial phase (i.e., start-up) of the epoxidation process is provided. The HSC conditioning process of the present disclosure ensures that the heat release from a catalyst bed containing an HSC during a start-up operation is less than 2000 kJ/Kgcat·hr. The HSC containing catalyst bed that has been conditioned by the process of the present disclosure exhibits improved performance (i.e., EO selectivity) and reduced hot spots.
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公开(公告)号:US20240024857A1
公开(公告)日:2024-01-25
申请号:US17867950
申请日:2022-07-19
Applicant: Scientific Design Company, Inc.
Inventor: Xiankuan Zhang , Christelle Verrier
Abstract: A conditioning process that is employed with a high selectivity catalyst (HSC) during an initial phase (i.e., start-up) of the epoxidation process is provided. The HSC conditioning process of the present disclosure ensures that the heat release from a catalyst bed containing an HSC during a start-up operation is less than 2000 kJ/Kgcat·hr. The HSC containing catalyst bed that has been conditioned by the process of the present disclosure exhibits improved performance (i.e., EO selectivity) and reduced hot spots.
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公开(公告)号:US10040055B2
公开(公告)日:2018-08-07
申请号:US15579419
申请日:2016-06-02
Applicant: SCIENTIFIC DESIGN COMPANY, INC.
Inventor: Christelle Verrier , Wojciech L. Suchanek
IPC: B01J21/04 , B01J21/08 , B01J21/12 , B01J23/04 , B01J23/36 , B01J23/50 , B01J35/10 , B01J19/00 , C07D301/10 , B01J37/00
Abstract: A method is provided for improving the performance of a silver-based epoxidation catalyst comprising a carrier. The carrier includes at least 80 percent alpha alumina and has a pore volume from 0.3 mL/g to 1.2 mL/g, a surface area from 0.3 m2/g to 3.0 m2/g, and a pore architecture that provides at least one of a tortuosity of 7 or less, a constriction of 4 or less and a permeability of 30 mdarcys or greater. A catalytic amount of silver and a promoting amount of one or more promoters is disposed on and/or in said carrier. The method further includes the steps of initiating an epoxidation reaction by reacting a feed gas composition containing ethylene and oxygen present in a ratio of from about 3.5:1 to about 12:1, in the presence of the silver-based epoxidation catalyst at a temperature of about 200° C. to about 230° C., and subsequently increasing the temperature either stepwise or continuously.
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