摘要
MoO3在CH4/H2气氛中程序升温还原碳化反应制备了Mo2C催化剂,用XRD、BET、SEM、XPS进行了表征。以吡啶/环己烷溶液为模型化合物,在高压微反装置上评价了碳化钼催化剂的吡啶加氢脱氮性能。结果表明,MoO3在CH4/H2气氛中程序升温至675℃可制得高纯度的β-Mo2C,SEM表征其形貌为板块状颗粒,平均粒径约3.9μm,比表面积达到了10.7m2/g,高于其前驱体MoO3的2.7倍。在反应压力3.0MPa,空速为8h-1,H2/原料液体积比为500:1,体积分数为5%的吡啶/环己烷溶液中,碳化钼催化剂在340℃下的吡啶加氢脱氮转化率达到了86.30%,高于相应MoS2约8%。随还原碳化温度的升高,碳化钼催化剂的比表面积降低,表面积炭增多,导致其吡啶加氢脱氮活性下降。确定的碳化钼催化剂的合成条件以还原碳化温度675℃、还原碳化气体空速1.8×104h-1左右较为适宜。
Molybdenum carbide catalysts were prepared through temperature-programmed carburization of molybdenum trioxide with CH4/H2 gas mixture and characterized by XRD, BET, SEM, and XPS. The hydrodenitrogenation (HDN) performance of the molybdenum carbide catalyst was evaluated by using 5 % pyridine/cyclohexane as a model reactant. The β-Mo2C prepared ( carburized at 675 ℃ ) is in high purity with an average dimension of about 3.9 μm; its BET surface area is 10.7 m^2/g, which is 2.7 times higher than that of MoO3. Over MOEC, pyridine HDN conversion reaches 86.30% under 340 ℃, 3.0 MPa, and a space velocity 8 h^-1, which is about 8 percentages higher than that over MoS2. The optimal carburizing conditions for preparing MOEC are around 675 ℃ with a CH4/H2 gas velocity of about 1.8 × 10^4 h^-1. Further increase of carburizing temperature may result in a decrease of the BET surface area of MOEC and an increase of free carbon content deposited on the catalyst surface, which can then decrease the HDN activity of MOEC.
出处
《燃料化学学报》
EI
CAS
CSCD
北大核心
2008年第1期89-93,共5页
Journal of Fuel Chemistry and Technology
基金
国家重点基础研究发展规划(973计划
G2000048003)
关键词
碳化钼
加氢脱氮
碳化
吡啶
molybdenum carbide
hydrodenitrogenation
carburization
pyridine