Agglomerated alumina-based spherical grains
    41.
    发明授权
    Agglomerated alumina-based spherical grains 失效
    聚集的氧化铝基球形颗粒

    公开(公告)号:US3960772A

    公开(公告)日:1976-06-01

    申请号:US455233

    申请日:1974-03-27

    Abstract: The invention concerns alumina-based spherically shaped grains produced from pastes of moistened particles. These grains are produced by subjecting the pastes, in the form of grains of any shape whatever, to the action of mechanical vibrations of frequencies within the range of from a few herz, in liquids which are slightly or not at all water-miscible. To the alumina, which is the main component, particles of various natures and acids, bases and various compounds which are dissolved in the water used for preparing the pastes, can be added. Once matured, dried and calcined, the grains have a very high level of resistance to attrition, a porosity comprising pores of large dimensions, and can be used in particular for adsorption, chromatography and catalysis.

    Abstract translation: 本发明涉及由湿润颗粒糊制成的氧化铝基球形颗粒。 这些颗粒是通过将任何形状的颗粒形式的糊状物在少量或不完全与水混溶的液体中经受几毫升范围内的频率的机械振动的作用而制得的。 作为主要成分的氧化铝可以添加各种性质的酸和碱,溶解在用于制备糊料的水中的各种化合物。 一旦成熟,干燥和煅烧,颗粒具有非常高的耐磨性,具有包括大尺寸的孔的孔隙率,并且可以特别用于吸附,色谱和催化。

    SELECTIVE SURFACE IMPREGNATION METHOD FOR CATALYTICALLY ACTIVE MATERIALS ON PARTICULATE CATALYST SUPPORT USING MUTUAL REPULSIVE FORCE AND SOBLUBILITY DIFFERENCE BETWEEN HYDROPHILIC SOLVENT AND HYDROPHOBIC SOLVENT
    48.
    发明申请
    SELECTIVE SURFACE IMPREGNATION METHOD FOR CATALYTICALLY ACTIVE MATERIALS ON PARTICULATE CATALYST SUPPORT USING MUTUAL REPULSIVE FORCE AND SOBLUBILITY DIFFERENCE BETWEEN HYDROPHILIC SOLVENT AND HYDROPHOBIC SOLVENT 审中-公开
    选择性表面曝光方法,用于催化活性材料的催化剂支持使用相互作用力和氢化溶剂和疏水溶剂之间的可溶性差异

    公开(公告)号:US20170072385A1

    公开(公告)日:2017-03-16

    申请号:US15343360

    申请日:2016-11-04

    Abstract: A method for preparing a catalyst having catalytically active materials selectively impregnated or supported only in the surface region of the catalyst particle using the mutual repulsive force of a hydrophobic solution and a hydrophilic solution and the solubility difference to a metal salt precursor between the hydrophobic and hydrophilic solutions. The hydrophobic solvent is a C2-C6 alcohol. The hydrophobic solvent is introduced into the catalyst support and then removed of a part of the pores connected to the outer part of the catalyst particle by drying under appropriate conditions. Then, a hydrophilic solution containing a metal salt is introduced to occupy the void spaces removed of the hydrophobic solvent, and the catalyst particle is dried at a low rate to selectively support or impregnate the catalytically active material or the precursor of the catalytically active material only in the outer part of the catalyst particle.

    Abstract translation: 一种制备具有催化活性物质的催化剂的方法,其使用疏水溶液和亲水溶液的相互排斥力选择性地浸渍或仅负载在催化剂颗粒的表面区域中,并且与疏水性和亲水性之间的金属盐前体的溶解度差异 解决方案 疏水性溶剂是C2-C6醇。 将疏水性溶剂引入催化剂载体中,然后通过在合适的条件下干燥除去连接到催化剂颗粒的外部的一部分孔。 然后,引入含有金属盐的亲水性溶液以占据除去疏水性溶剂的空隙空间,并且催化剂颗粒以较低的速率被干燥以选择性地仅支持或浸渍催化活性材料或催化活性材料的前体 在催化剂颗粒的外部。

    Catalytic composition for the electrochemical reduction of carbon dioxide
    50.
    发明授权
    Catalytic composition for the electrochemical reduction of carbon dioxide 有权
    用于电化学还原二氧化碳的催化组合物

    公开(公告)号:US09333487B2

    公开(公告)日:2016-05-10

    申请号:US14539508

    申请日:2014-11-12

    Abstract: The catalytic composition for the electrochemical reduction of carbon dioxide is a metal oxide supported by multi-walled carbon nanotubes. The metal oxide may be nickel oxide (NiO) or tin dioxide (SnO2). The metal oxides form 20 wt % of the catalyst. In order to make the catalysts, a metal oxide precursor is first dissolved in deionized water to form a metal oxide precursor solution. The metal oxide precursor solution is then sonicated and the solution is impregnated in a support material composed of multi-walled carbon nanotubes to form a slurry. The slurry is then sonicated to form a homogeneous solid solution. Solids are removed from the homogeneous solid solution and dried in an oven for about 24 hours at a temperature of about 110° C. Drying is then followed by calcination in a tubular furnace under an argon atmosphere for about three hours at a temperature of 450° C.

    Abstract translation: 用于二氧化碳的电化学还原的催化组合物是由多壁碳纳米管支撑的金属氧化物。 金属氧化物可以是氧化镍(NiO)或二氧化锡(SnO 2)。 金属氧化物形成20重量%的催化剂。 为了制备催化剂,首先将金属氧化物前体溶解在去离子水中以形成金属氧化物前体溶液。 然后将金属氧化物前体溶液超声处理,并将溶液浸渍在由多壁碳纳米管组成的载体材料中以形成浆料。 然后将浆液超声处理以形成均匀的固溶体。 将固体从均匀的固溶体中除去,并在烘箱中在约110℃的温度下干燥约24小时。然后在管式炉中在氩气气氛下在450℃的温度下煅烧约3小时 C。

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