Propane oxidative dehydrogenation over VOx/SBA-15 catalysts

被引:38
|
作者
Mitran, Gheorghita [1 ]
Ahmed, Rawaz [2 ,3 ]
Iro, Emmanuel [2 ]
Hajimirzaee, Saeed [2 ]
Hodgson, Simon [2 ]
Urda, Adriana [1 ]
Olea, Maria [2 ]
Marcu, Ioan-Cezar [1 ]
机构
[1] Univ Bucharest, Fac Chem, Dept Organ Chem Biochem & Catalysis, Lab Chem Technol & Catalysis, 4-12 Blv Regina Elisabeta, Bucharest 030018, Romania
[2] Teesside Univ, Sch Sci & Engn, Middlesbrough, Cleveland, England
[3] Kurdistan Inst Strateg Studies & Sci Res KISSR, Slemani, As Sulaymaniyah, Iran
关键词
Oxidative dehydrogenation; Propane; Supported vanadia catalysts; VOx/SBA-15; VANADIUM-OXIDE CATALYSTS; MESOPOROUS SBA-15; N-BUTANE; SILICA SBA-15; MIXED OXIDES; ALKANES; PERFORMANCE; REACTIVITY; DISPERSION; KINETICS;
D O I
10.1016/j.cattod.2016.12.014
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
VOx/SBA-15 catalysts with five different vanadium loadings were prepared by a modified wet impregnation method, characterized using N-2 adsorption, XRD, EDX, SEM, Raman and UV-vis spectroscopies and H-2-TPR techniques, and tested in the oxidative dehydrogenation of propane in the temperature range 450-600 degrees C. For all the catalysts the propane conversion increases with both reaction temperature and vanadium loading, while the selectivity for propene decreases mainly to the benefit of carbon oxides. Several types of VOx species coexist on the catalyst surface, with monomeric and low-polymerized ones leading mainly to propene, while V2O5 crystallites at high vanadium loadings producing more carbon oxides. Propene was determined to be the only primary product irrespective of the vanadium content. (C) 2016 Elsevier B.V. All rights reserved.
引用
收藏
页码:260 / 267
页数:8
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