Oxidative steam reforming of ethanol for hydrogen production was studied over 1%Rh/CeO2Al2O3 catalyst prepared in the laboratory. Support with CeO2 content of 5wt% on γ -Al2O3 was prepared by impregnation with Ce(NO3)3.6H2O solution. The effects of temperature (450°C and 550°C), Water/Ethanol ratio (mol/mol) (3 and 8) and Oxygen/Ethanol molar ratio (0.23 and 0.3) were studied at 1 atmospheric pressure in a down-flow tubular fixed bed reactor. The percentage conversion of ethanol ranged from 90% to 98% and maximum hydrogen selectivity was observed up to 70% at a selected Water /Oxygen/Ethanol molar ratio at 550°C. On increasing Water/Ethanol molar ratios in the feed, the catalytic activity for hydrogen production could be enhanced.
Tengfei HouBo YuShaoyin ZhangTongkuan XuDazhi WangWeijie Cai
Tarak MondalKamal Kishore PantAjay K. Dalai
Weijie CaiBaocai ZhangYong LiYide XuWenjie Shen
Tarak MondalKamal Kishore PantAjay K. Dalai