Production of linear alkyl benzene
    1.
    发明申请
    Production of linear alkyl benzene 有权
    生产线性烷基苯

    公开(公告)号:US20070038007A1

    公开(公告)日:2007-02-15

    申请号:US10549768

    申请日:2004-03-10

    IPC分类号: C07C13/00 C07C4/00

    摘要: This invention relates to a process for producing linear alkyl benzene, the process including the steps of obtaining a hydrocarbon condensate containing olefins, paraffins and oxygenates from a low temperature Fischer-Tropsch reaction; a) fractionating a desired carbon number distribution from the hydrocarbon condensate to form a fractionated hydrocarbon condensate stream; b) extracting oxygenates from the fractionated hydrocarbon condensate stream from step (a) to form a stream containing olefins and paraffins; c) combining the stream containing olefins and paraffins from step (b) with the feed stream from step (g) to form a combined stream; d) alkylating olefins in the combined stream from step (c) with benzene in the presence of a suitable alkylation catalyst in an alkylation reactor, e) recovering linear alkyl benzene from the alkylation reactor; f) recovering unreacted paraffins from the alkylation reactor; g) dehydrogenating the unreacted paraffins in the presence of a suitable dehydrogenation catalyst to form a feed stream containing olefins and paraffins; and h) sending the feed stream containing olefins and paraffins from step (g) to step (c).

    摘要翻译: 本发明涉及一种直链烷基苯的制备方法,该方法包括以下步骤:从低温费 - 托反应获得含有烯烃,链烷烃和含氧化合物的烃缩合物; a)从烃缩合物中分馏所需的碳数分布以形成分馏的烃冷凝物流; b)从步骤(a)的分馏的烃冷凝物流中提取含氧化合物以形成含有烯烃和链烷烃的物流; c)将来自步骤(b)的含有烯烃和链烷烃的料流与来自步骤(g)的进料流混合以形成组合料流; d)在烷基化反应器中,在合适的烷基化催化剂存在下,将来自步骤(c)的合并物流中的烯烃与苯烷基化,e)从烷基化反应器回收直链烷基苯; f)从烷基化反应器回收未反应的链烷烃; g)在合适的脱氢催化剂存在下使未反应的链烷烃脱氢以形成含有烯烃和链烷烃的进料流; 和h)将来自步骤(g)的含有烯烃和链烷烃的进料流送至步骤(c)。