Heterogeneous arylalkyl oxidation promoter
    1.
    发明申请
    Heterogeneous arylalkyl oxidation promoter 失效
    异构芳烷基氧化促进剂

    公开(公告)号:US20080319234A1

    公开(公告)日:2008-12-25

    申请号:US11821020

    申请日:2007-06-21

    摘要: A promoter can have utility in selective heterogeneous oxidation of arylalkyl hydrocarbons such as, for example, cyclohexyl benzene and/or sec-butyl benzene to form hydroperoxides. The promoter can include the product of contacting a solid support comprising a metal oxide surface and an iron compound. The solid support can include, for example, titanium dioxide and/or an iron oxide such as magnetite and can have magnetic susceptibility. A method for the oxidation of arylalkyl hydrocarbons to form hydroperoxides can include contacting 16 an arylalkyl hydrocarbon with oxygen in the presence of the promoter under catalytic oxidation conditions to form arylalkyl hydroperoxide, which can then be converted to phenol via cleavage 26. The method can include recovery 22 of the promoter from the arylalkyl hydroperoxide and can further include recycling the recovered promoter to the contacting 16. Where the solid support has magnetic susceptibility, the recovery 22 can include magnetic separation of the promoter.

    摘要翻译: 助催化剂可用于芳基烷基烃例如环己基苯和/或仲丁基苯的选择性异相氧化以形成氢过氧化物。 助催化剂可以包括使包含金属氧化物表面和铁化合物的固体载体接触的产物。 固体支持体可以包括例如二氧化钛和/或氧化铁如磁铁矿,并且可以具有磁化率。 用于氧化芳基烷基烃以形成氢过氧化物的方法可以包括在催化氧化条件下在助催化剂存在下使芳烷基烃与氧接触,形成芳基烷基氢过氧化物,然后可通过裂解将其转化为苯酚。该方法可包括 从芳基烷基氢过氧化物中回收22个启动子,并且可以进一步包括将回收的促进剂再循环到接触16.当固体支持物具有磁化率时,回收22可以包括促进剂的磁性分离。

    Heterogeneous arylalkyl oxidation promoter
    2.
    发明授权
    Heterogeneous arylalkyl oxidation promoter 失效
    异构芳烷基氧化促进剂

    公开(公告)号:US07692046B2

    公开(公告)日:2010-04-06

    申请号:US11821020

    申请日:2007-06-21

    IPC分类号: C07C409/00

    摘要: A promoter can have utility in selective heterogeneous oxidation of arylalkyl hydrocarbons such as, for example, cyclohexyl benzene and/or sec-butyl benzene to form hydroperoxides. The promoter can include the product of contacting a solid support comprising a metal oxide surface and an iron compound. The solid support can include, for example, titanium dioxide and/or an iron oxide such as magnetite and can have magnetic susceptibility. A method for the oxidation of arylalkyl hydrocarbons to form hydroperoxides can include contacting 16 an arylalkyl hydrocarbon with oxygen in the presence of the promoter under catalytic oxidation conditions to form arylalkyl hydroperoxide, which can then be converted to phenol via cleavage 26. The method can include recovery 22 of the promoter from the arylalkyl hydroperoxide and can further include recycling the recovered promoter to the contacting 16. Where the solid support has magnetic susceptibility, the recovery 22 can include magnetic separation of the promoter.

    摘要翻译: 助催化剂可用于芳基烷基烃例如环己基苯和/或仲丁基苯的选择性异相氧化以形成氢过氧化物。 助催化剂可以包括使包含金属氧化物表面和铁化合物的固体载体接触的产物。 固体支持体可以包括例如二氧化钛和/或氧化铁如磁铁矿,并且可以具有磁化率。 用于氧化芳基烷基烃以形成氢过氧化物的方法可以包括在催化氧化条件下在助催化剂存在下使芳烷基烃与氧接触,形成芳基烷基氢过氧化物,然后可通过裂解将其转化为苯酚。该方法可包括 从芳基烷基氢过氧化物中回收22个启动子,并且可以进一步包括将回收的促进剂再循环到接触16.当固体支持物具有磁化率时,回收22可以包括促进剂的磁性分离。

    Process of producing cyclohexylbenzene
    10.
    发明授权
    Process of producing cyclohexylbenzene 有权
    生产环己基苯的方法

    公开(公告)号:US09365467B2

    公开(公告)日:2016-06-14

    申请号:US13883742

    申请日:2011-12-02

    摘要: In a process for producing cyclohexylbenzene, benzene is contacted with hydrogen under hydroalkylation conditions effective to form a first effluent stream comprising cyclohexylbenzene, cyclohexane, methylcyclopentane, and unreacted benzene. At least a portion of the first effluent stream is contacted with a dehydrogenation catalyst under dehydrogenation conditions to convert at least a portion of the cyclohexane to benzene thereby forming a second effluent stream. The amount of methylcyclopentane in the second effluent stream is different by no more than 65% of the total amount of the portion of the first effluent stream, said amounts being on a weight basis. A methylcyclopentane-containing stream is removed from either the first or the second effluent stream and at least a portion of the second effluent stream containing benzene is recycled to the hydroalkylation step.

    摘要翻译: 在生产环己基苯的方法中,苯在有效形成包含环己基苯,环己烷,甲基环戊烷和未反应苯的第一流出物流的加氢烷基化条件下与氢气接触。 在脱氢条件下,将至少一部分第一流出物流与脱氢催化剂接触以将至少一部分环己烷转化为苯,从而形成第二流出物流。 第二流出物流中的甲基环戊烷的量不同于第一流出物流的部分总量的不超过65%,所述量基于重量。 从第一或第二流出物流中除去含甲基环戊烷的物流,并将含有苯的第二流出物流的至少一部分再循环至加氢烷基化步骤。