V2O5负载量对VOx/MgAl2O4催化异丁烷脱氢制异丁烯的影响

采用浸渍法制备了不同V2O5负载量VOx/MgAl2O4催化剂，考察了该系列催化剂在560 °C时的异丁烷脱氢反应性能。利用XRD、低温氮气吸脱附、FT-IR和H2-TPR等分析手段对催化剂的性质进行了表征，并分析了催化剂表面性质与其催化性能的关系。结果表明：当V2O5负载量（w）低于5 %时，催化剂表面以还原性能好、单层分散的孤立态和聚合态钒氧物种为主；当V2O5负载量高于5 wt%时，催化剂表面开始形成还原性能较差的镁钒酸盐物种。异丁烷脱氢反应活性结果表明，当V2O5负载量（w）为5 %时，异丁烷脱氢性能最佳，异丁烷转化率和异丁烯收率可分别达到41.9 %和31.4 %。低价态钒氧物种为异丁烷脱氢反应的活性物种。

INFLUENCE OF V2O5 LOADING ON ISOBUTANE DEHYDROGENATION ON VOx/MgAl2O4 CATALYST

VOx/MgAl2O4 catalysts with different V2O5 loadings were prepared by the incipient wetness impregnation and their isobutane dehydrogenation activities were investigated. X-ray diffraction (XRD), nitrogen adsorption-desorption, Fourier transform infrared (FT-IR) spectroscopy and hydrogen-temperature programmed reduction (H2-TPR) were used to characterize the structure and reducibility of vanadium species on the surface of MgAl2O4. The results show that the isolated and polymeric VO4 species on the surface are present at low vanadium loading of <5% and can be reduced more easily than samples with higher vanadium loading. With increase of V2O5 loadings, mixed magnesium vanadate compounds (Mg3V2O8, Mg2V2O7) appear, which are difficult to reduce by hydrogen. At the optimum V2O5 loading (5%), yield of isobutylene was 31.4% with the corresponding isobutane conversion of about 41.9% at 560 ℃，reaction time 1.5h. Based on the experimental results, it is suggested that low valence Vδ+ (δ<5) species on the surface are the active sites for this reaction..