Evolution of active catalysts for the selective oxidative dehydrogenation of methanol on Fe2O3 surface doped with Mo oxide

被引:35
作者
Bowker, M. [1 ,2 ]
Brookes, C. [1 ,2 ]
Carley, A. F. [1 ]
House, M. P. [1 ]
Kosif, M. [1 ,3 ]
Sankar, G. [2 ,4 ]
Wawata, I. [1 ]
Wells, P. P. [2 ,4 ]
Yaseneva, P. [1 ]
机构
[1] Cardiff Univ, Sch Chem, Cardiff Catalysis Inst, Cardiff CF10 3AT, S Glam, Wales
[2] Rutherford Appleton Lab, Res Complex Harwell RCaH, Harwell OX11 0F, Oxon, England
[3] Marmara Univ, Dept Chem, Istanbul, Turkey
[4] UCL, Dept Chem, London WC1E 6BT, England
基金
英国工程与自然科学研究理事会;
关键词
IRON MOLYBDATE CATALYSTS; MOLYBDENUM TRIOXIDE; CALCINATION TEMPERATURE; FE CATALYSTS; FORMALDEHYDE; RAMAN; SPECTROSCOPY; SYSTEM;
D O I
10.1039/c3cp50399b
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070305 [高分子化学与物理];
摘要
Iron molybdate catalysts are used for the selective oxidation of methanol to formaldehyde. In this paper we have attempted to understand what determines high selectivity in this reaction system by doping haematite with surface layers of Mo by incipient wetness impregnation. This works well and the Mo appears to form finely dispersed layers. Even very low loadings of Mo have a marked effect on improving the selectivity to formaldehyde. Haematite itself is a very poor catalyst with high selectivity to combustion products, whereas, when only 0.25 monolayers of Mo are deposited on the surface, formaldehyde and CO selectivities are greatly enhanced and CO2 production is greatly diminished. However, even with as much as seven monolayers of Mo dosed on to the surface, these materials achieve much less selectivity to formaldehyde at high conversion than do the industrial catalysts. The reason for this is that the Mo forms a 'skin' of ferric molybdate on a core of iron oxide, but does not produce a pure Mo oxide monolayer on the surface, a situation which is essential for very high yields of formaldehyde.
引用
收藏
页码:12056 / 12067
页数:12
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