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    Reactor for chemical conversion of a feed with added heat, and crosswise flow of feed and catalyst
    1.
    发明申请
    Reactor for chemical conversion of a feed with added heat, and crosswise flow of feed and catalyst 有权
    用于加热进料的化学转化反应器，以及进料和催化剂的横向流动

    公开(公告)号：US20060216218A1

    公开(公告)日：2006-09-28

    申请号：US11442328

    申请日：2006-05-30

    申请人： Eric Lenglet ,  Nicolas Boudet ,  Frederic Hoffmann

    发明人： Eric Lenglet ,  Nicolas Boudet ,  Frederic Hoffmann

    IPC分类号： B01J8/08

    CPC分类号： B01J8/0496 ,  B01J8/0438 ,  B01J8/12

    摘要： A chemical conversion reactor contains a substantially vertical catalytic bed between an upper end and a lower end and comprises, in combination: close to its upper end, at least one means for introducing a solid catalyst, means for introducing and evacuating said feed allowing its flow in a substantially horizontal direction through the catalytic bed, means for heating said feed integrated into said reactor, said reactor comprising, close to its lower end, at least one means for extraction of the catalyst, which extraction is differentiated between an upstream portion and a downstream portion of said catalytic bed, with respect to the direction of flow of said feed.

    摘要翻译： 化学转化反应器在上端和下端之间包含基本上垂直的催化床，其组合包括：靠近其上端的至少一个用于引入固体催化剂的装置，用于引入和排空所述进料允许其流动的装置 在通过催化床的基本上水平的方向上，用于加热集成到所述反应器中的所述进料的装置，所述反应器包括靠近其下端的至少一个用于萃取催化剂的装置，所述提取在上游部分和 所述催化床的下游部分相对于所述进料的流动方向。

    Process for the production of synthesis gas with conversion of CO2 into hydrogen
    8.
    发明申请
    Process for the production of synthesis gas with conversion of CO2 into hydrogen 有权
    用CO 2转化为氢气生产合成气的方法

    公开(公告)号：US20090012188A1

    公开(公告)日：2009-01-08

    申请号：US11890525

    申请日：2007-08-07

    申请人： Alexandre Rojey ,  Reynald Bonneau ,  Nicolas Boudet

    发明人： Alexandre Rojey ,  Reynald Bonneau ,  Nicolas Boudet

    IPC分类号： C07C27/00

    CPC分类号： C01B3/36 ,  C01B2203/0233 ,  C01B2203/0255 ,  C01B2203/062 ,  C10J3/00 ,  C10J3/82 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/093 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  C10K3/026 ,  Y02E50/18 ,  Y02P20/129 ,  Y02P20/145 ,  Y02P20/146

    摘要： Process for the production of liquid hydrocarbons from a feedstock that comprises at least one elementary feedstock from the group of biomass, coal, lignite, petroleum residues, methane, and natural gas, comprising: at least one stage a) for gasification of the feedstock by partial oxidation and/or steam reforming to produce a synthesis gas SG; a stage b) for separating CO2 from SG and a portion of the effluent of the subsequent stage c); the mixing of a portion of the CO2 that is separated with a gas of an H2/CO ratio of more than 3; a stage c) for partial conversion with hydrogen, thermal or thermocatalytic, of the CO2 that is present in said first mixture according to the reaction: CO2+H2→CO+H2O in a specific reaction zone that is separated from said gasification zone or zones; a stage d) for Fisher-Tropsch synthesis on a synthesis gas that comprises at least a portion of SG and at least a portion of the CO that is produced by the conversion of CO2 into hydrogen.

    摘要翻译： 用于从原料生产液体烃的方法，所述原料包含来自生物质，煤，褐煤，石油残渣，甲烷和天然气组的至少一种基本原料，包括：至少一个阶段a）用于通过 部分氧化和/或蒸汽重整以产生合成气SG; 一个阶段b）从SG和后续阶段c）的一部分流出物分离CO 2; 将一部分与H2 / CO比大于3的气体分离的CO 2混合; 根据CO 2 + H 2→CO + H 2 O在与所述气化区分离的特定反应区中，存在于所述第一混合物中的CO 2部分转化为氢，热或热催化的阶段c） 区域 合成气中的Fisher-Tropsch合成阶段d），其包含至少一部分SG和通过CO 2转化为氢而产生的至少一部分CO。