Behavior of steam reforming reaction for bio-ethanol over Pt/ZrO2 catalysts

被引:51
作者
Yamazaki, Tatsuya [1 ]
Kikuchi, Naoko [1 ]
Katoh, Masahiro [2 ]
Hirose, Toyoko [1 ]
Saito, Hiroaki [3 ]
Yoshikawa, Takushi [4 ]
Wada, Mamoru [4 ]
机构
[1] Ishinomaki Senshu Univ, Fac Sci & Engn, Dept Basic Sci, Ishinomaki, Miyagi 9868580, Japan
[2] Univ Tokushima, Inst Sci & Technol, Dept Adv Mat, Tokushima 7708506, Japan
[3] Tohoku Univ, Grad Sch Engn, Aoba Ku, Sendai, Miyagi 9808579, Japan
[4] Sanwa Cornstarch Co Ltd, Nara 6348585, Japan
关键词
Bio-ethanol; Ethanol steam reforming; Platinum catalyst; Hydrogen formation; Deactivation; HYDROGEN-PRODUCTION; LOW-TEMPERATURE; BIOETHANOL; OXIDE; BIOMASS; OIL; NI; CO;
D O I
10.1016/j.apcatb.2010.06.003
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Steam reforming reactions of reagent ethanol and of biomass-derived ethanol (bio-ethanol) over Pt catalysts supported on ZrO2 were studied. For steam reforming reactions at 673 K of reagent ethanol with an H2O/C2H5OH molar ratio = 3, the initial H-2 yields were 20-29%. The major carbon-containing products were CH4, CO2, and CO. Small amounts of acetaldehyde, acetone, and ethylene were produced, showing that the partial ethanol steam reforming reaction (C2H5OH + H2O -> CH4 + CO2 + 2H(2)) occurred competitively with the ethanol decomposition reaction (C2H5OH -> CH4 + CO+ H-2). H-2 formation for bio-ethanol was less than that obtained with reagent ethanol under the same conditions. The catalytic activity for the partial steam reforming reaction decreased rapidly; a similar decrease in the activity of the ethanol decomposition reaction was observed. The poisoning effect of sulfur compounds on the Pt sites was responsible for the deactivation of the bio-ethanol steam reforming reaction. (C) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:81 / 88
页数:8
相关论文
共 24 条
[1]   Synthesis, characterization and performance evaluation of Ni/Al2O3 catalysts for reforming of crude ethanol for hydrogen production [J].
Akande , AJ ;
Idem, RO ;
Dalai, AK .
APPLIED CATALYSIS A-GENERAL, 2005, 287 (02) :159-175
[2]   Biomass gasification to hydrogen and syngas at low temperature: Novel catalytic system using fluidized-bed reactor [J].
Asadullah, M ;
Ito, S ;
Kunimori, K ;
Yamada, M ;
Tomishige, K .
JOURNAL OF CATALYSIS, 2002, 208 (02) :255-259
[3]   Bio-ethanol catalytic steam reforming over supported metal catalysts [J].
Auprêtre, F ;
Descorme, C ;
Duprez, D .
CATALYSIS COMMUNICATIONS, 2002, 3 (06) :263-267
[4]   Ethanol steam reforming over MgxNi1-xAl2O3 spinel oxide-supported Rh catalysts [J].
Aupretre, F ;
Descorme, C ;
Duprez, D ;
Casanave, D ;
Uzio, D .
JOURNAL OF CATALYSIS, 2005, 233 (02) :464-477
[5]   Low temperature catalytic steam reforming of ethanol. 2. Preliminary kinetic investigation of Pt/CeO2 catalysts [J].
Ciambelli, P. ;
Palma, V. ;
Ruggiero, A. .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2010, 96 (1-2) :190-197
[6]   Bio-ethanol steam reforming on Ni/Al2O3 catalyst [J].
Comas, J ;
Mariño, F ;
Laborde, M ;
Amadeo, N .
CHEMICAL ENGINEERING JOURNAL, 2004, 98 (1-2) :61-68
[7]   Hydrogen production by ethanol steam reforming over a commercial Pd/-γ-Al2O3 catalyst [J].
Goula, MA ;
Kontou, SK ;
Tsiakaras, PE .
APPLIED CATALYSIS B-ENVIRONMENTAL, 2004, 49 (02) :135-144
[8]   Current status of hydrogen production techniques by steam reforming of ethanol: A review [J].
Haryanto, A ;
Fernando, S ;
Murali, N ;
Adhikari, S .
ENERGY & FUELS, 2005, 19 (05) :2098-2106
[9]  
*JASO, 2006, M36106 JASO
[10]   Efficient production of hydrogen over supported cobalt catalysts from ethanol steam reforming [J].
Llorca, J ;
Homs, N ;
Sales, J ;
de la Piscina, PR .
JOURNAL OF CATALYSIS, 2002, 209 (02) :306-317