摘要
采用浸渍法制备了一系列NiM/γ-Al2O3(M=Mo、W)催化剂.通过馏分油(沸点70 ℃~350 ℃)烯烃的加氢饱和,考察了Mo、W对Ni基催化剂加氢性能的影响,并采用TPR、XRD、XPS对催化剂进行表征.TPR结果表明,添加助剂Mo(W)降低了低温还原峰温度,但还原度有所降低,而且NiMo催化剂还原度的降低幅度比NiW催化剂更大;XRD结果表明,Mo(W)的添加提高了活性组分Ni的分散度,并且Mo的助分散作用优于W;XPS结果表明,Mo(W)的引入提高了催化剂体系'表面NiAl2O4'的比例,Ni2p3/2谱峰的化学位移说明助剂的添加增强了Ni与载体γ-Al2O3之间的相互作用.
A series of alumina supported Ni,Mo-Ni and W-Ni catalysts were prepared by co-impregnation and the structure and nickel species were characterized by XRD,TPR and XPS.The effect of additive Mo(W) on catalyst activity for the hydrogenation of olefins in the fraction(boiling spread: 70 ℃~350 ℃) was studied.TPR characterization reveals the addition of additives shifts the high-temperature reduced peak to higher temperature but the low-temperature reduced peak to lower one.For the decrease of deoxidizing temperature,the effect of Mo is better than that of W.XRD measurements show that Mo and W increase the dispersion of NiO on the supports in the order of Mo>W.XPS analyse reveals the ratio of surface NiAl2O4 increases due to the presence of Mo and W.The shift of Ni2p3/2 peak indicates a stronger interaction between the NiO and γ-Al2O3 support.
出处
《燃料化学学报》
EI
CAS
CSCD
北大核心
2007年第5期595-598,共4页
Journal of Fuel Chemistry and Technology
基金
国家高技术研究发展规划(863计划
2001AA523010)