ZnO和MoO3掺杂对氧化铝负载氧化锰体系表面和催化性能的影响

S. M. Ibrahim, G. El-Shobaky, G. M. Mohamed, N. Hassan
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引用次数: 4

摘要

以Al(OH)3细粉和计算量的Mn(NO3)2溶解在最少量蒸馏水中,通过浸渍法制备Mn2O3/Al2O3体系,然后在400-600℃烘干煅烧。用不同量的Zn(NO3)2或(NH4)6Mo7O24.4H2O浸渍Al(OH)3粉末,干燥后再浸渍Mn(NO3)2,制备了6种掺杂固体。将掺杂固体在400-600℃下煅烧。ZnO和MoO3的掺杂浓度分别为0.75、1.5和3 mol%。采用XRD、- 196℃氮气吸附和常压下140 ~ 280℃流动技术对纯固体和不同掺杂固体的结构特征、表面和催化性能进行了表征。结果表明:所研究的纯固体和掺杂0.75和1.5mol% ZnO或MoO3的固体在500℃下煅烧后,由纳米MnO2(软锰矿)和Mn2O3 (Partridgeite相)以及al -Al2O3组成。将不同掺杂固体的煅烧温度提高到600℃,可以使MnO2(软锰矿)完全转化为纳米级的Mn2O3 (Partridgeite相)。锰氧化物相的晶粒尺寸在3 ~ 56 nm之间。煅烧温度和掺杂剂浓度对体系的所有表面特性都有很大影响。在不同温度下煅烧的纯体系和掺杂体系上进行异丙醇转化,分别通过脱水和脱氢生成丙烯和丙酮。反应温度、煅烧温度和掺杂浓度对各种固体的活性和选择性影响较大。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Effects of ZnO and MoO3 Doping on Surface and Catalytic Properties of Manganese Oxide Supported on Alumina System
Mn2O3/Al2O3 system was prepared by the impregnation method using finely powdered Al(OH)3 and a calculated amount of Mn(NO3)2 dissolved in the smallest amount of distilled water followed by drying and calcination at 400-600°C. Six doped solids were prepared by impregnating powdered Al(OH)3 Solids with different amounts of Zn(NO3)2 or (NH4)6Mo7O24.4H2O followed by drying, then impregnating with Mn(NO3)2. The doped solids were calcined at 400-600°C. The dopant concentrations were 0.75, 1.5, and 3 mol% ZnO or MoO3. The structural characteristics, surface and the catalytic properties of pure and variously doped solids were examined by using XRD, N2 adsorption at- 196°C and isopropanol conversion carried out at 140-280°C using a flow technique under atmospheric pressure. The obtained results revealed that the pure solids investigated and those doped with 0.75 and 1.5mol% ZnO or MoO3 calcined at 500°C, consisted of a mixture of nanosized MnO2 (Pyrolusite) and Mn2O3 (Partridgeite phase) together with � -Al2O3. Increasing the calcination temperature of the variously doped solids to 600°C led to the complete conversion MnO2(Pyrolusite) to nanosized Mn2O3 (Partridgeite phase). The crystallite size of manganese oxide phases varied between 3 and 56 nm. All surface characteristics of the system investigated were much affected by calcination temperature and dopant concentration. Isopropanol conversion carried out over pure and doped system calcined at different temperatures proceeded via dehydration and dehydrogenation yielding propene and acetone, respectively. The activity and selectivity of the various solids were much affected by the reaction temperature, calcination temperature and dopant concentration.
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