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机构地区:[1]中国科学院山西煤炭化学研究所煤转化国家重点实验室
出 处:《燃料化学学报》1994年第3期264-268,共5页Journal of Fuel Chemistry and Technology
摘 要:以沥青中间相为原料,氢氧化钾直接活化,获得了比表面达2363m ̄2/g的超高比表面炭分子筛(CMS)。分别以CMS、SiO_2、活性炭和θ-Al_2O_3为担体,制备了负载钼催化剂,并研究其加压甲烷化反应性能,发现活性依下面顺序增加:θ-Al_2O_3<SiO_2<活性炭(AC)<CMS。还分别以钼酸铵和磷钼酸(HPMo)为前驱体,制备了CMS负载钼催化剂,并考察了其煤气甲烷化活性,发现不同的催化剂前驱体对催化剂反应活性影响很大。根据产物中CH_4/CO_2的变化,推测CO在钼催化剂上的甲烷化反应包括如下两个步骤:(1)3H_2+CO→CH_4+H_2O,(2)CO+H_2O→CO_2+H_2。A unique carbon molecular sieve(CMS)having an ultra-high surface areahigher than 2300m ̄2/g was developed. The carbon material was made by a direct chemical ac-tivation process in which mesophase pitch was reacted with excess KOH. Several molydenumcatalysts supporded on θ-Al_2O_3、 SiO_2,activated carbon and CMS were prepared and theircatalytic performances in the methanation of CO were examined.The catalytic activities in-creased in the following sequence:θ-Al_2O_3<SiO_2<activated carbon<CMS. Two catalystswith HPMo and(NH_4)_6Mo_7O_(24)·2H_2O as precursors were prepared and tested for their usein the methanation of CO. The results show that the activity of HPMo/CMS for CO metha-nation was much higher than that of MoO_3/CMS.Comparing the ratios of CH_4/CO_2 in reac-tion products,it is suggested that the methanation of CO on molybdenum catalysts proceedsthrough two steps:(1)CO+3H_2→CH_4+H_2O;(2)CO+H_2O→CO_2+H_2
分 类 号:TQ544[化学工程—煤化学工程]
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