%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