%0 Journal Article %T Experimental study on catalytic hydrogasification of lignite
褐煤催化加氢气化实验研究 %A ZHAN Shu-peng %A WANG Xing-jun %A HONG Bing-qing %A YU Guang-suo %A WANG Fu-chen %A
战书鹏 %A 王兴军 %A 洪冰清 %A 于广锁 %A 王辅臣 %J 燃料化学学报 %D 2012 %I %X Effect of alkali metal K on the hydrogasification of lignite was studied in a pressurized fixed-bed reactor,and the effects of temperature,pressure and catalyst loading on the reactivity of hydrogasification of lignite coal were examined.The experimental results show that the alkali metal K has a superior catalysis on the hydrogasification of lignite,and the carbon conversion of hydrogasification and the methane content in gaseous products can be up to 95% and 89%,respectively.The gasification reactivity can be enhanced obviously by increasing temperature,pressure and catalyst loading,and the catalyst loading saturation level is about 15%.The surface morphology and pore structure of coal samples with different catalyst loadings have been analyzed using scanning electron microscope(SEM) and gas adsorption/desorption analysis,which indicates that the specific surface areas and total pore volume decrease initially,and then increase with the increasing of catalyst loading. %K alkali metal %K fixed-bed reactor %K catalytic gasification %K hydrogasification
碱金属 %K 固定床 %K 催化气化 %K 加氢气化 %U http://www.alljournals.cn/get_abstract_url.aspx?pcid=6E709DC38FA1D09A4B578DD0906875B5B44D4D294832BB8E&cid=6579068328FE643F&jid=C6AB115B41BD2F1616ECDB095B69B8ED&aid=EC09C1218AC1072B41E53503D98ED401&yid=99E9153A83D4CB11&vid=1371F55DA51B6E64&iid=CA4FD0336C81A37A&sid=5D311CA918CA9A03&eid=F3583C8E78166B9E&journal_id=0253-2409&journal_name=燃料化学学报&referenced_num=0&reference_num=15