Particulate solids for catalyst supports and heat transfer materials
    3.
    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

    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
    4.
    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

    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。

    Rhodium recovery process
    10.
    发明授权
    Rhodium recovery process 失效
    铑恢复过程

    公开(公告)号:US4363765A

    公开(公告)日:1982-12-14

    申请号:US250614

    申请日:1981-04-03

    摘要: A particular process is provided for the recovery of rhodium values from liquid compositions. The process comprises contacting a solubilized rhodium complex with water, a crown ether and an alkaline cesium salt in the liquid phase such that a solid comprising rhodium is formed. The process is applied with particular advantage to the recovery of solubilized rhodium values derived from processes for the production of polyhydric alcohols such as ethylene glycol, and monohydric alcohols such as methanol, by the reaction of carbon monoxide and hydrogen in the presence of rhodium carbonyl complex catalysts in a homogeneous liquid medium. The invention also concerns cesium/crown ether salts of anionic rhodium complexes.

    摘要翻译: 提供了从液体组合物中回收铑值的具体方法。 该方法包括使溶解的铑配合物与水,冠醚和碱铯盐在液相中接触,使得形成包含铑的固体。 该方法特别有利于通过一氧化碳和氢在铑羰基络合物的存在下,通过一氧化碳和氢气的反应回收衍生自多元醇如乙二醇和一元醇如甲醇的溶解的铑值 催化剂在均匀的液体介质中。 本发明还涉及阴离子铑络合物的铯/冠醚盐。