摘要
采用浸渍法制备了LiLaNi/Al2O3催化剂,并用XRD,SEM,TPR等对其进行了表征.Li的加入对催化剂的结构、NiAl2O4的结晶度及Ni2+离子还原能力都有较大影响.以甲苯为焦油的模型化合物,在固定床反应器中对高温焦炉煤气中焦油催化转化反应进行了评价.结果显示,Li能显著改善LaNi/Al2O3催化剂的催化反应活性,提高产物中H2的含量.在750℃、水/碳比为2.0的条件下,含0.5%(ω)Li的LiLaNi/Al2O3催化剂能将甲苯完全转化为小分子气体,产物中H2含量显著增加.
The catalytic activity of LiLaNi/Al2O3 was evaluated in a fixed-bed reactor via steam reforming of toluene as a model tar compound. The results showed that addition of Li could improve the catalytic activity of LiLaNi/Al2O3 and enhance H2 content in the resultant gas mixture. XRD, SEM and TPR results illustrated that the addition of Li had great influence on the structure of LiLaNi/Al2O3 catalysts and the reduction ability of Ni^2+ ions. The catalyst 0.5LiLaNi/Al2O3 possessed the optimal catalytic performance. LiLaNi/Al2O3 also showed good resistance to coking for steam reforming of tar at a high temperature of 750 ℃.
出处
《过程工程学报》
CAS
CSCD
北大核心
2009年第2期403-407,共5页
The Chinese Journal of Process Engineering
基金
国家高技术研究发展计划(863)基金资助项目(编号:2006AA11A189)
上海市科学技术委员会重点基金资助项目(编号:06DZ12212)
先进钢铁材料技术国家工程研究中心研究基金资助项目(编号:中050209)