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    Process for the preparation of high activity carbon monoxide hydrogenation catalysts; the catalyst compositions, use of the catalysts for conducting such reactions, and the products of such reactions
    1.
    发明授权
    Process for the preparation of high activity carbon monoxide hydrogenation catalysts; the catalyst compositions, use of the catalysts for conducting such reactions, and the products of such reactions 有权
    制备高活性一氧化碳氢化催化剂的方法; 催化剂组合物，用于进行这种反应的催化剂的使用以及这些反应的产物

    公开(公告)号：US06331574B1

    公开(公告)日：2001-12-18

    申请号：US09415084

    申请日：1999-10-08

    申请人： Albert L'Vovoch Lapidus ,  Alla Jurievna Krylova ,  Michel A. Daage ,  Russell J. Koveal ,  Rocco A. Fiato

    发明人： Albert L'Vovoch Lapidus ,  Alla Jurievna Krylova ,  Michel A. Daage ,  Russell J. Koveal ,  Rocco A. Fiato

    IPC分类号： C07C2700

    CPC分类号： C10G2/332 ,  B01J29/90 ,  B01J37/06 ,  B01J38/50 ,  B01J38/66 ,  C07C1/0445 ,  C07C1/045 ,  C07C2529/08 ,  C07C2529/18 ,  C07C2529/70 ,  C07C2529/83 ,  C07C2529/85 ,  Y02P20/584

    摘要： A process for the preparation of a catalyst useful for conducting carbon monoxide hydrogenation reactions, especially Fischer-Tropsch reactions. The steps of the process begin with the activation, or reactivation, of a deactivated catalyst, or with the preparation and activation of a fresh catalyst. In accordance with the latter, the steps of the process comprise, first contacting, in one or more steps, a powder or preformed, particulate refractory inorganic support with a liquid, or solution in which there is dispersed or dissolved a compound, or salt of a catalytically active metal, or metals, to impregnate and deposit the metal, or metals, upon the support, or powder. The metal, or metals, impregnated support is calcined following each impregnation step to form oxides of the deposited metal, or metals. The calcined catalyst precursor is then treated with a solution of a chelating compound, preferably a poly- or multidentate chelating compound, sufficient to complex with, extract and remove a portion of the oxides of the metal, or metals. The catalyst is activated by reduction; suitably by contact with hydrogen. In the activation, or reactivation of a deactivated catalyst, the catalyst is first treated with the chelating compound to extract a portion of the oxides of the metal, or metals, and the catalyst is then reduced. In either event, the activated or reactivated catalyst has high activity, or high C5+ selectivity, or both high activity and C5+ selectivity in conducting carbon monoxide hydrogenation reactions. The productivity of the process is increased.

    摘要翻译： 一种制备可用于进行一氧化碳氢化反应，特别是费 - 托反应的催化剂的方法。 该方法的步骤开始于失活催化剂的活化或再活化，或与新鲜催化剂的制备和活化。 根据后者，该方法的步骤包括首先在一个或多个步骤中接触粉末或预成型的颗粒状耐火无机载体与液体或其中分散或溶解化合物或其中的化合物或 催化活性金属或金属，以将金属或金属浸渍并沉积在载体或粉末上。 在每个浸渍步骤之后煅烧金属或金属浸渍的载体以形成沉积的金属或金属的氧化物。 然后将煅烧的催化剂前体用螯合化合物，优选多齿螯合化合物的溶液处理，该溶液足以与金属或金属的一部分氧化物复合，提取和除去。 催化剂通过还原活化; 适当地通过与氢接触。 在失活的催化剂的活化或再活化中，催化剂首先用螯合化合物处理以提取一部分金属或金属的氧化物，然后还原催化剂。 在任一情况下，活化或再活化的催化剂在进行一氧化碳氢化反应时具有高活性或高C5 +选择性，或高活性和C5 +选择性。 该过程的生产率增加。

    Particulate solids for catalyst supports and heat transfer materials
    4.
    发明授权
    Particulate solids for catalyst supports and heat transfer materials 失效
    用于催化剂载体和传热材料的颗粒状固体

    公开(公告)号：US5476877A

    公开(公告)日：1995-12-19

    申请号：US346973

    申请日：1994-11-29

    申请人： LeRoy R. Clavenna ,  Stephen M. Davis ,  Rocco A. Fiato ,  Geoffrey R. Say

    发明人： LeRoy R. Clavenna ,  Stephen M. Davis ,  Rocco A. Fiato ,  Geoffrey R. Say

    IPC分类号： B01J21/06 ,  B01J23/83 ,  C01B3/40 ,  C07C27/00

    CPC分类号： B01J21/066 ,  B01J23/83 ,  C01B3/40 ,  C01B2203/1052 ,  C01B2203/1064 ,  C01B2203/1082 ,  Y02P20/52

    摘要： A particulate, precalcined low silica content zirconia, especially one stabilizer with yttria, is useful as a catalyst support or as a heat transfer solids component for conducting chemical reactions at high temperature, in oxidizing, reducing or hydrothermal conditions, especially in syn gas operations. An admixture of precalcined particulate low silica content zirconia, particularly a low silica content yttria-stabilized zirconia, is employed in a preferred embodiment as a heat transfer solid, in concentrations ranging generally from about 10 wt. % to about 99.9 wt. % with a particulate catalyst notably a nickel-on-alumina catalyst, in concentration ranging generally from about 0. 1 wt. % to about 90 wt. %. Such an admixture provides a particularly useful catalytic contact mass in high temperature oxidizing, reducing and hydrothermal environments, notably in conducting synthesis gas generation operations. This type of bed promotes continuous, highly efficient heat and mass transfer within the reacting gas phase. The presence of the heat transfer solid as a bed component maintains excellent bed fluidization characteristics, suppressing the normal tendency of the catalyst to sinter or agglomerate; tendencies which promote defluidization of the bed. Moreover, the heat transfer particles of the bed are highly attrition resistant, and are chemically compatible with the catalyst particles of the admixture.

    摘要翻译： 颗粒状预煅烧的低二氧化硅含量的氧化锆，特别是具有氧化钇的一种稳定剂，可用作催化剂载体或用作在高温，氧化，还原或水热条件下进行化学反应的传热固体组分，特别是在合成气操作中。 预先煅烧的颗粒状低二氧化硅含量的氧化锆，特别是低二氧化硅含量氧化钇稳定的氧化锆的混合物在优选的实施方案中用作传热固体，浓度通常为约10重量％ ％至约99.9wt。 ％的颗粒催化剂，特别是镍 - 氧化铝催化剂，其浓度范围通常为约0.1重量％ ％至约90wt。 ％。 这种混合物在高温氧化，还原和水热环境中特别是在进行合成气生成操作中提供特别有用的催化接触物质。 这种类型的床促进在反应气相内的连续，高效的热和质量传递。 作为床成分的传热固体的存在保持了优异的床流化特性，抑制了催化剂烧结或附聚的正常趋势; 促进床层流变的趋势。 此外，床的传热颗粒是高度耐磨性的，并且与混合物的催化剂颗粒化学相容。

    Synthesis gas from particulate catalysts, and admixtures of particulate catalysts and heat transfer solids
    5.
    发明授权
    Synthesis gas from particulate catalysts, and admixtures of particulate catalysts and heat transfer solids 失效
    颗粒催化剂的合成气，颗粒催化剂和传热固体的混合物

    公开(公告)号：US5348717A

    公开(公告)日：1994-09-20

    申请号：US60332

    申请日：1993-05-11

    申请人： LeRoy R. Clavenna ,  Stephen M. Davis ,  Geoffrey R. Say ,  Rocco A. Fiato

    发明人： LeRoy R. Clavenna ,  Stephen M. Davis ,  Geoffrey R. Say ,  Rocco A. Fiato

    IPC分类号： B01J37/04 ,  C01B3/40 ,  C01B3/44 ,  C01B32/40 ,  C01B3/02 ,  C01B3/26 ,  C01B31/18

    CPC分类号： B01J37/04 ,  C01B3/40 ,  C01B3/44 ,  C01B31/18 ,  C01B2203/1052 ,  C01B2203/1064 ,  C01B2203/1082 ,  Y02P20/52

    摘要： A process utilizing a particulate catalyst, or particulate catalyst admixed with particulate heat transfer solids for conducting high temperature fluidized bed syn gas operations. Hydrogen and carbon monoxide are produced from a low molecular weight hydrocarbon by contact thereof, at high temperature in the presence of oxygen, or steam and oxygen, with a fluidized bed comprising said particulate solids. In one of its forms, barium hexaluminate is employed as a heat transfer solid, in concentrations ranging generally from about 10 wt. % to about 99.9 wt. %, in admixture with a particulate catalyst containing a metal, or metals, component catalytic for the production of hydrogen and carbon monoxide from low molecular weight hydrocarbons contacted with a fluidized bed of the catalyst at high temperature hydrothermal conditions. The catalyst, suitably one having a barium hexaluminate carrier component, is employed in concentration ranging generally from about 0.1 wt. % to about 90 wt. %. Such an admixture provides a particularly useful catalytic contact mass for conducting fluidized bed synthesis gas generation operations. This type of bed promotes continuous, highly efficient heat and mass transfer within the reacting gas phase. The presence of the catalyst having a barium hexaluminate carrier component, or barium hexaluminate heat transfer solid as a bed component maintains excellent bed fluidization characteristics, suppressing the normal tendency of the catalyst to sinter or agglomerate; tendencies which promote defluidization of the bed. Moreover, the heat transfer particles of the bed are highly attrition resistant, and are chemically compatible with the catalyst particles of the admixture.

    摘要翻译： 一种利用颗粒催化剂或与颗粒状传热固体混合的颗粒催化剂进行高温流化床合成气操作的方法。 氢和一氧化碳通过与低分子量烃在氧气或蒸气和氧气的存在下在高温下与其接触而产生，其中包含所述颗粒固体的流化床。 在其一种形式中，采用六铝酸钡作为传热固体，其浓度通常为约10wt。 ％至约99.9wt。 ％，与含有金属或金属的颗粒催化剂的混合物，催化剂用于在高温水热条件下与催化剂的流化床接触的低分子量烃生产氢气和一氧化碳。 合适地使用具有六铝酸钡载体组分的催化剂的浓度通常为约0.1重量％ ％至约90wt。 ％。 这种混合物提供用于进行流化床合成气产生操作的特别有用的催化接触物质。 这种类型的床促进在反应气相内的连续，高效的热和质量传递。 作为床成分的具有六铝酸钡载体成分或六铝酸钡传热固体的催化剂的存在保持了优异的床流化特性，抑制了催化剂烧结或附聚的正常趋势; 促进床层流变的趋势。 此外，床的传热颗粒是高度耐磨性的，并且与混合物的催化剂颗粒化学相容。