发明申请
- 专利标题: METHOD FOR PRODUCING OXIDIZED OLEFIN THROUGH OLEFIN EPOXIDATION
- 专利标题(中): 通过烯烃环氧化生产氧化烯烃的方法
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申请号: US13878659申请日: 2011-10-11
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公开(公告)号: US20130211112A1公开(公告)日: 2013-08-15
- 发明人: Hua Li , Min Lin , Xiaoju Wu , Wei Wang , Chijian He , Jizao Gao , Xingtian Shu , Shuanghua Wan , Bin Zhu
- 申请人: Hua Li , Min Lin , Xiaoju Wu , Wei Wang , Chijian He , Jizao Gao , Xingtian Shu , Shuanghua Wan , Bin Zhu
- 申请人地址: CN Beijing
- 专利权人: CHINA PETROLEUM & CHEMICAL CORPORATION
- 当前专利权人: CHINA PETROLEUM & CHEMICAL CORPORATION
- 当前专利权人地址: CN Beijing
- 优先权: CN201010511515.X 20101011; CN201010511561.X 20101011
- 国际申请: PCT/CN11/01703 WO 20111011
- 主分类号: C07D301/12
- IPC分类号: C07D301/12
摘要:
A process for producing an alkylene oxide by olefin epoxidation, wherein said process comprises the steps of: (1) in a first olefin epoxidation condition, in the presence of a first solid catalyst, a first mixed stream containing a solvent, an olefin and H2O2 is subjected to an epoxidation in one or more fixed bed reactors and/or one or more moving bed reactors until the conversion of H2O2 reaches 50%-95%, then, optionally, the resulting reaction mixture obtained in the step (1) is subjected to a separation to obtain a first stream free of H2O2 and a second stream containing the unreacted H2O2, and the olefin is introduced to the second stream to produce a second mixed stream, or optionally, the olefin is introduced to the reaction mixture obtained in the step (1) to produce a second mixed stream; (2) in a second olefin epoxidation condition, the reaction mixture obtained in the step (1) or the second mixed stream obtained in the step (1) and a second solid catalyst are introduced to one or more slurry bed reactors to conduct an epoxidation until the total conversion of H2O2 reaches 98% or more, with a proviso that said process for producing the alkylene oxide by olefin epoxidation has an selectivity for the alkylene oxide of 90% or more.The process of the present invention combines the slurry bed reactor with the fixed bed reactor and/or the moving bed reactor so as to overcome the disadvantages of the low conversion of H2O2 in the case that only the fixed bed reactor and/or the moving bed reactor are used, and the low selectivity for the target alkylene oxide in the case that only the slurry bed reactor is used.
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