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Iron molybdate catalysts for methanol to formaldehyde oxidation:effects of Mo excess o catalytic behaviour

机译:钼酸铁催化剂催化甲醇氧化甲醛的反应:过量钼对催化行为的影响

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Two iron molybdate catalysts have been prepared by coprecipitation, one stoichiometric (Mo/Fe atomic ratio= 1.5) and the other with a typical industrial composition (Mo/Fe atomic ratio=3). Physicochemical characterisation shows that Mo excess brings about an increase in the surface area and deconvolution of NH3 TPD curves evidences some changes in acidity. On the other hand, surprisingly, Mo excess does not cause significant changes in the activity for methanol oxidation per unit surface area. This provides evidence that Fe2(MoO4)3 is in fact the active phase of the catalyst. The catalyst with Mo excess leads to higher selectivity for HCHO to the detriment of dimethyl ether selectivity. This result is attributable to larger oxygen availability at the catalyst surface and changes in acidity. The catalytic behaviour of the prepared catalysts was compared with that of an industrial catalyst. It was found that the prepared catalyst with an Mo/Fe composition similar to the industrial one is more active due to larger surface area.
机译:通过共沉淀制备了两种钼酸铁催化剂,一种是化学计量的(Mo / Fe原子比= 1.5),另一种具有典型的工业组成(Mo / Fe原子比= 3)。理化特性表明,过量的Mo导致表面积增加,NH3 TPD曲线的反卷积表明酸度有所变化。另一方面,令人惊讶地,过量的Mo不会引起单位表面积的甲醇氧化活性的显着变化。这提供了证据,即Fe2(MoO4)3实际上是催化剂的活性相。 Mo过量的催化剂导致对HCHO的更高的选择性,从而损害了二甲醚的选择性。该结果归因于催化剂表面上更大的氧可利用性和酸度的变化。将制备的催化剂与工业催化剂的催化行为进行比较。已经发现,由于具有较大的表面积,因此所制得的具有类似于工业用Mo / Fe组成的催化剂更具活性。

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