Iso/normal paraffin separation by membrane extraction
    15.
    发明授权
    Iso/normal paraffin separation by membrane extraction 失效
    Iso /正常石蜡分离膜提取

    公开(公告)号:US5107059A

    公开(公告)日:1992-04-21

    申请号:US622689

    申请日:1990-12-05

    CPC classification number: C07C7/144

    Abstract: Non-normal, branched paraffins (isoparaffins) are separated from hydrocarbon feeds comprising mixtures of isoparaffins and normal paraffins by the procedure involving the steps of contacting the hydrocarbon feed with one face of a non-selective, microporous partition barrier membrane while simultaneously contacting the opposite face of said membrane, preferably in countercurrent flow, with a polar solvent. The isoparaffins in the feed selectively permeate across the porous partition barrier membrane in response to the polar solvent to the solvent side of the membrane whereby a permeate enriched in isoparaffins and a retentate of decreased isoparaffin content as compared to the feed are obtained.

    Abstract translation: 通过包括使烃进料与非选择性微孔隔壁隔离膜的一面接触的步骤,将包含异链烷烃和正链烷烃的混合物的非正构支链烷烃(异链烷烃)与包含异链烷烃和正链烷烃的混合物分离,同时使相反的 所述膜的表面,优选以逆流流动,与极性溶剂反应。 进料中的异链烷烃选择性渗透多孔分隔阻隔膜,以响应于极性溶剂到膜的溶剂侧,从而获得富含异链烷烃的渗透物和与进料相比降低的异链烷烃含量的渗余物。

    Selective separation of naphthenes from paraffins by membrane extraction
    16.
    发明授权
    Selective separation of naphthenes from paraffins by membrane extraction 失效
    通过膜萃取从石蜡中选择性分离环烷烃

    公开(公告)号:US5107056A

    公开(公告)日:1992-04-21

    申请号:US622442

    申请日:1990-12-05

    CPC classification number: C10G31/11 C07C7/144

    Abstract: Naphthenic hydrocarbons are separated from aliphatic rich hydrocarbon feeds comprising mixtures of naphthenes with paraffinic hydrocarbons by a membrane extraction process whereby the hydrocarbon feed is contacted with one face of a porous, non-selective partition barrier membrane while simultaneously contacting the other side of said membrane with a polar solvent such as ethylenediamine. The naphthenic hydrocarbon preferentially migrates through the porous membrane partition barrier in response to the polar solvent present on the permeate side of the barrier.

    Abstract translation: 环烷烃通过膜提取方法从包含环烷烃与链烷烃的混合物的富含脂肪烃的进料中分离,由此烃进料与多孔非选择性分隔壁隔膜的一面接触,同时使所述膜的另一侧与 极性溶剂如乙二胺。 响应于存在于屏障的渗透侧的极性溶剂,环烷烃优先通过多孔膜隔离屏障迁移。

    Process of producing cyclohexylbenzene
    18.
    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

    Abstract: 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.

    Abstract translation: 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。

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