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Metal-support interactions in Pt/Al2O3 and Pd/Al2O3 catalysts for CO oxidation

机译:Pt / Al2O3和Pd / Al2O3催化剂中的金属-载体相互作用用于CO氧化

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Platinum and palladium catalysts supported on γ-Al2O3 were studied by XRD, UV-vis DRS, HRTEM, TPR-H2, XPS together with measurements of their catalytic properties. The properties of the catalysts denoted as Pt(Pd)/Al2O3(X)-Y (X-the calcination temperature of support, °C; Y- the calcination temperature of cat-alyst,°C) were studied as a function of the temperatures used for calcination of the support and/or the catalyst in oxygen or in a reaction mixture of CO + O2. It was found that the deposition of Pt or Pd on γ-Al2O3 did not alter the structure of the support. Two types of the Pt and Pd particles were typically present on the γ-AI2O3 surface: individual particles with dimensions of 1.5-3 nm and agglomerates about 100 nm in size. In the catalysts calcined at relatively low temperatures (Pt/Al2O3(550)-450), platinum was present in the form of metal clusters. However, in the Pd/Al2O3(550)-450 catalyst, the palladium particles were almost completely decorated with a thin layer of an aluminate phase. These structures are not reduced in hydrogen in the temperature range of -15 to 450 °C, and are stable to treatment in a reaction mixture of CO + O2. Pd deposition on the γ-Al2O3-800 support was found to result in stabilization of the active component in two main forms, Pd° and PdO, with varying degrees of interaction due to the decoration effect. Calcination at the low temperature of 550 °C led to the formation of a so-called "core-shell structure", where a palladium metal core is covered with a thin shell of an aluminate phase. Depending on the calcination temperature of the catalyst in the range of 450-1000°C, the morphological form of the active component was converted from the "core-shell" state to a state consisting of two phases, Pd° and PdO, with a gradual decrease of the Pd°/PdO ratio, weakening the interaction with the support and the growth of palladium particles. Under the action of the reaction mixture, the Pd/Al2O3(800)-(450,600,800,1000) catalysts underwent changes in the Pd°/PdO ratio, which regulates the light-off temperature. After catalyst calcination at the highest temperature used in this study, 1200°C, the palladium particles became much larger due to the loss of the palladium interaction with the support. Only the metal phase of palladium was observed in these catalysts, and their catalytic activity decreases substantially.
机译:通过XRD,UV-vis DRS,HRTEM,TPR-H2,XPS研究了负载在γ-Al2O3上的铂和钯催化剂及其催化性能。研究了以Pt(Pd)/ Al2O3(X)-Y(X-载体的煅烧温度,°C; Y-催化剂的煅烧温度,°C)为代表的催化剂的性能。在氧气或CO + O2的反应混合物中煅烧载体和/或催化剂所用的温度。发现Pt或Pd在γ-Al2 O 3上的沉积不会改变载体的结构。 γ-Al2O3表面通常存在两种类型的Pt和Pd颗粒:尺寸为1.5-3 nm的单个颗粒和团聚体,尺寸约为100 nm。在相对较低的温度(Pt / Al2O3(550)-450)下煅烧的催化剂中,铂以金属簇的形式存在。但是,在Pd / Al2O3(550)-450催化剂中,钯颗粒几乎被铝酸盐相的薄层完全装饰。这些结构在-15至450°C的温度范围内不会被氢还原,并且对于在CO + O2的反应混合物中处理稳定。发现Pd沉积在γ-Al2O3-800载体上可以使活性成分稳定在两种主要形式中,即Pd°和PdO,由于装饰效果,相互作用程度不同。在550℃的低温下煅烧导致形成所谓的“核-壳结构”,其中钯金属核被铝酸盐相的薄壳覆盖。根据催化剂的煅烧温度在450-1000°C范围内,活性成分的形态从“核-壳”状态转变为由Pd°和PdO两相组成的状态, Pd°/ PdO比值逐渐降低,削弱了与载体的相互作用以及钯颗粒的生长。在反应混合物的作用下,Pd / Al2O3(800)-(450,600,800,1000)催化剂的Pd°/ PdO比发生变化,从而调节起燃温度。在本研究中使用的最高温度1200°C下催化剂煅烧后,由于钯与载体的相互作用丧失,钯颗粒变得更大。在这些催化剂中仅观察到钯的金属相,并且它们的催化活性大大降低。

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