利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

6 条记录 (耗时 0.039 秒)

    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：US20070066859A1

    公开(公告)日：2007-03-22

    申请号：US10549769

    申请日：2004-03-10

    申请人： Edward Koper ,  Ivan Greager ,  Jan Scholtz ,  Johan Wet ,  Mieke Desmet ,  Wilhelmina Jansen ,  Paul Jacobson

    发明人： Edward Koper ,  Ivan Greager ,  Jan Scholtz ,  Johan Wet ,  Mieke Desmet ,  Wilhelmina Jansen ,  Paul Jacobson

    IPC分类号： C07C2/68

    CPC分类号： C07C2/66 ,  C07C15/02

    摘要： This invention relates to a process for producing linear alkyl benzene and linear paraffins, 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) alkylating the stream containing olefins and paraffins from step b) with benzene in the presence of a suitable alkylation catalyst; and d) recovering linear alkyl benzene and linear paraffin.

    摘要翻译： 本发明涉及直链烷基苯和直链烷烃的制备方法，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）从来自步骤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）在合适的烷基化催化剂存在下，用苯将来自步骤b）的含有烯烃和链烷烃的物流烷基化; 和d）回收直链烷基苯和线型石蜡。

    Method of purifying fischer-tropsch derived water
    5.
    发明申请
    Method of purifying fischer-tropsch derived water 有权
    费 - 托衍生水的纯化方法

    公开(公告)号：US20050131084A1

    公开(公告)日：2005-06-16

    申请号：US11014517

    申请日：2004-12-16

    申请人： Luis Kohler ,  Gert du Plessis ,  Francois Toit ,  Edward Koper ,  Trevor Phillips ,  Janette Walt

    发明人： Luis Kohler ,  Gert du Plessis ,  Francois Toit ,  Edward Koper ,  Trevor Phillips ,  Janette Walt

    IPC分类号： C02F3/04 ,  B01D11/04 ,  B01D61/14 ,  C02F1/04 ,  C02F1/26 ,  C02F3/00 ,  C02F3/08 ,  C02F3/12 ,  C02F3/28 ,  C02F5/06 ,  C02F9/00 ,  C02F9/02 ,  C02F9/14 ,  C07C51/44 ,  C07C51/48 ,  C07C53/08 ,  C07C53/122 ,  C07C53/124 ,  C07C53/126 ,  C07C27/26

    CPC分类号： C02F9/00 ,  C02F1/04 ,  C02F1/26 ,  C02F3/00 ,  C02F2101/32 ,  C02F2101/34

    摘要： A process for the production of purified water from Fischer-Tropsch reaction water wherein the purified water is an aqueous stream having a COD of between 20 and 500 mg/l, a pH of between 6.0 and 9.0, a suspended solids content of less than 250 mg/l and a total dissolved solids content of less than 600 mg/l, and wherein the process includes at least the steps of a primary treatment stage comprising an equilibrium staged separation process having at least one stage for removing at least a fraction of non-acid oxygenated hydrocarbons from the Fischer-Tropsch reaction water to produce a primary water enriched stream, a secondary treatment stage comprising liquid-liquid extraction for removing at least a fraction of organic acids from at least a portion of the primary water enriched stream to produce a secondary water enriched stream, a tertiary treatment stage comprising biological treatment for removing at least a fraction of acidic oxygenated hydrocarbons from at least a portion of the secondary water enriched stream to produce a tertiary water enriched stream and a quartic treatment stage comprising solid-liquid separation for removing at least some solids from at least a portion of the tertiary water enriched stream.

    摘要翻译： 用于从费 - 托反应水生产纯净水的方法，其中纯化水是COD为20-500mg / l，pH为6.0-9.0，悬浮固体含量小于250 mg / l，总溶解固体含量小于600mg / l，并​​且其中该方法至少包括主要处理阶段的步骤，所述初级处理阶段包括平衡分级分离方法，该方法具有至少一个阶段，用于除去至少一部分非 - - 来自费 - 托反应水的含氧烃，以产生初级富水流，二级处理阶段包括液 - 液萃取，用于从至少一部分初级富水流中除去至少一部分有机酸，以产生 第二富水流，第三处理阶段包括用于从至少一部分所述至少一部分去除至少一部分酸性氧化烃的生物处理 第二富水流以产生富含三水的料流和四次处理阶段，其包括固液分离，用于从至少一部分富含水的料流中除去至少一些固体。