Char as catalyst for hydrogen production by glycerol reforming

• 作 者: ZhangZhikai;ChengLiang;CaiXuan;SunJianlei;WangChaoxun;XuQingli;ZhangSuping;YanYongjie;
• 机 构: Research Center for Biomass Energy,East China University of Science and Technology,Shanghai,China
• 出 处: The 4th International Conference on Biomass Energy Technolog
• 发表日期: 2014年期

　　Hydrogen production from the steam reforming reaction of glycerol has been studied over char as catalyst in tubular fixed bed reactor.The effects of operating parameters such as temperature,steam/carbon ratio(S/C)and WHSV on hydrogen yield and carbon conversion was examined under atmospheric pressure.The result showed that carbon conversion increase with the increase of temperature and S/C.Ultimately,hydrogen yield and potential hydrogen yield were up to 72.16%and 81.28%,as well as the carbon conversion reached 89.08%at 800℃,S/C=4:1 and WHSV=1.5 h-1.