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Thermally stable supported metal catalysts and inorganic membranes prepared by sol-gel processing.

机译:通过溶胶-凝胶工艺制备的热稳定负载型金属催化剂和无机膜。

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The application of sol-gel processing to the synthesis of supported metal catalysts, inorganic membranes and catalytic membranes was studied. Noble metals were supported on SiO2 and gamma-Al2O 3. These materials have high surface areas, well-defined pore size distributions, and average pore diameters around 4 nm. The effects of preparative variables such as pH, gelation temperature, metal precursor, metal loading and binder addition on the final properties of the materials were studied. The structure of the sol-gel derived support materials was used to stabilize the dispersion of the supported metal at elevated temperatures and enhance activity and selectivity of the catalyst.;The thermal stability of a sol-gel Rh/SiO2 catalyst was tested at 650°C in flowing O2 and compared to the stability of a similar sample prepared by the traditional method of ion-exchange. The ion-exchanged sample had an average pore diameter of 24 nm. The metal particle size distribution of the sol-gel catalyst was more stable due to the smaller pore diameter of that catalyst. The sol-gel samples were more active in the dehydrogenation of n-butane than the ion-exchanged sample. A similar effect of pore size was found for Pd/gamma-Al2O3 catalysts sintered in H 2 at 650°C.;The Pd/gamma-Al2O3 catalysts were found to be very active hydrogenation catalysts but were not selective to partially hydrogenated products. A boehmite sol was used as a coating on a porous alpha-Al 2O3 substrate to form a gamma-Al2O3 membrane that could act as a diffusion barrier for gases. A catalytic membrane was formed by adding a soluble palladium compound to the sol. The Pd/gamma-Al 2O3 membrane was used successfully in the selective hydrogenation reactions of acetylene and 1,3-butadiene to produce ethylene and butenes. This was accomplished by premixing the alkyne or diene with H2 and passing it through the membrane wall, therefore reducing the contact time between the reactants and the catalyst.
机译:研究了溶胶-凝胶法在负载型金属催化剂,无机膜和催化膜合成中的应用。贵金属负载在SiO2和γ-Al2O3上。这些材料具有较高的表面积,明确的孔径分布以及4 nm左右的平均孔径。研究了制备变量(例如pH,胶凝温度,金属前体,金属负载量和粘合剂添加量)对材料最终性能的影响。溶胶-凝胶衍生的载体材料的结构用于在高温下稳定负载金属的分散并提高催化剂的活性和选择性。;溶胶/凝胶Rh / SiO2催化剂的热稳定性在650°C下进行了测试C在流动的O2中,并与通过传统离子交换方法制备的类似样品的稳定性进行了比较。离子交换样品的平均孔径为24 nm。溶胶-凝胶催化剂的金属粒度分布由于该催化剂的较小孔径而更稳定。溶胶-凝胶样品在正丁烷脱氢中比离子交换样品更具活性。对于在650°C下在H 2中烧结的Pd /γ-Al2O3催化剂,发现了相似的孔径影响;发现Pd /γ-Al2O3催化剂是非常活泼的加氢催化剂,但对部分加氢产物没有选择性。将勃姆石溶胶用作多孔α-Al2O3基材上的涂层,以形成可充当气体扩散屏障的γ-Al2O3膜。通过向溶胶中添加可溶性钯化合物来形成催化膜。 Pd /γ-Al2O3膜已成功用于乙炔和1,3-丁二烯的选择性加氢反应以生产乙烯和丁烯。这是通过将炔烃或二烯与H2预混合并使其穿过膜壁而完成的,从而减少了反应物与催化剂之间的接触时间。

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