TY - JOUR
T1 - Effect of calcium addition on catalytic ethanol steam reforming of Ni/Al2O3
T2 - II. Acidity/basicity, water adsorption and catalytic activity
AU - Choong, Catherine K.S.
AU - Huang, Lin
AU - Zhong, Ziyi
AU - Lin, Jianyi
AU - Hong, Liang
AU - Chen, Luwei
N1 - Funding Information:
We gratefully acknowledge the Agency of Science, Technology and Research (A*STAR), Singapore for its financial support.
PY - 2011/11/4
Y1 - 2011/11/4
N2 - The effect of Ca modification to Ni/Al2O3 catalysts in ethanol steam reforming was studied by using a 5-channel micro-reactor, in situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS), and temperature-programmed desorption (TPD) of probe molecules H2O, NH3, CO2 and ethanol. Both Al2O3 and Ca-modified Al2O3 supports are not catalytically active for the ethanol reforming. But in the presence of the active metal Ni, the catalytic performance of Ni/Ca-Al2O3 is far more superior to Ni/Al2O3 for low temperature H2 production. The introduction of Ca greatly reduces the acidity of Al2O 3, depressing ethanol dehydration and ethylene formation. It brings about positive attributes such as increasing water adsorption, providing Ni catalyst the proximity and abundance of adsorbed OH groups. The involvement of OH groups in the reactions in turn enhances the ethanol adsorption, stabilizes its adsorbate intermediates for further conversions to H2, CH 4 and CO2 at relatively low temperatures. This paper therefore serves to illustrate the importance of acidity and steam adsorption capacity in the design of the catalysts for ethanol steam reforming.
AB - The effect of Ca modification to Ni/Al2O3 catalysts in ethanol steam reforming was studied by using a 5-channel micro-reactor, in situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS), and temperature-programmed desorption (TPD) of probe molecules H2O, NH3, CO2 and ethanol. Both Al2O3 and Ca-modified Al2O3 supports are not catalytically active for the ethanol reforming. But in the presence of the active metal Ni, the catalytic performance of Ni/Ca-Al2O3 is far more superior to Ni/Al2O3 for low temperature H2 production. The introduction of Ca greatly reduces the acidity of Al2O 3, depressing ethanol dehydration and ethylene formation. It brings about positive attributes such as increasing water adsorption, providing Ni catalyst the proximity and abundance of adsorbed OH groups. The involvement of OH groups in the reactions in turn enhances the ethanol adsorption, stabilizes its adsorbate intermediates for further conversions to H2, CH 4 and CO2 at relatively low temperatures. This paper therefore serves to illustrate the importance of acidity and steam adsorption capacity in the design of the catalysts for ethanol steam reforming.
KW - Acidity
KW - Calcium oxide
KW - Ethanol
KW - Nickel catalyst
KW - Steam reforming
KW - Surface OH groups
KW - Water adsorption
UR - http://www.scopus.com/inward/record.url?scp=80053974858&partnerID=8YFLogxK
U2 - 10.1016/j.apcata.2011.08.038
DO - 10.1016/j.apcata.2011.08.038
M3 - 文章
AN - SCOPUS:80053974858
SN - 0926-860X
VL - 407
SP - 155
EP - 162
JO - Applied Catalysis A: General
JF - Applied Catalysis A: General
IS - 1-2
ER -