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Tungsten and Tungsten Carbide Supported on Activated Carbon: Surface Structues and Performance for Ethylene Hydrogenation

机译:活性炭负载的钨和碳化钨:乙烯加氢的表面结构和性能

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摘要

Tungsten catalysts supported on an activated carbon were prepared, with different metal loading, by using either ammonium tungstate or tungsten hexacarbonyl as metal precursor compounds. The catalysts so prepared were heat treated inH2 flow at 748 and 973 K or in He flow at 1223 K. The heat-treated catalysts were characterized by N2 adsorption at 77 K and mercury porosimetry , to determine their surface area and porosity, and by XPS and XRD, to evaluate the chemical state and dispersion of the active phase. phase composed of metallic tungsten and tungsten trioxide, whereas the treatment in He generated a mixture of metallic tungsten, tungsten carbide, and tungsten trioxide. The catalysts containing tungsten carbide were the most active in the hydrogenation of ethene, even at a temperature as low as 273 K, although their rate of deactivation was dependent on reaction temperature; the lower the reaction temperature, the higher the rate of deactivation.
机译:通过使用钨酸铵或六羰基钨作为金属前体化合物,制备了负载在活性炭上的钨催化剂,其金属负载量不同。如此制备的催化剂在748和973 K的H2气流中或在1223 K的He气流中进行热处理。热处理过的催化剂的特征在于77 K的N2吸附和水银孔隙率法,以确定其表面积和孔隙率,以及XPS和XRD,以评估活性相的化学状态和分散性。相由金属钨和三氧化钨组成,而在He中处理则生成金属钨,碳化钨和三氧化钨的混合物。含碳化钨的催化剂即使在低至273 K的温度下,在乙烯的氢化中也最具活性,尽管它们的失活速率取决于反应温度。反应温度越低,失活速率越高。

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