Hydrogen produced from ethanol for internal reforming molten carbonate fuel cell

被引:117
作者
Cavallaro, S
Mondello, N
Freni, S
机构
[1] Inst TAE, CNR, I-98126 Messina, Italy
[2] Univ Messina, Dipartimento Chim Ind & Ingn Mat, I-98166 Messina, Italy
关键词
steam reforming; hydrogen production; molten carbonate fuel cell; cobalt; rhodium; ethanol;
D O I
10.1016/S0378-7753(01)00800-X
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
Ethanol is, proposed as alternative fuel for the indirect internal reformer of molten carbonate fuel cells (IIR-MCFCs). At MCFCs, working conditions (T = 923 K and P = 1 bar), both Rh- and Co-based catalysts have been tested using diluted ethanol/water mixture. The steam/ carbon ratio of the feed was selected close to 4.2 mol/mol, in the aim to simulate the composition of ethanol/water mixture produced from biomasses. A good performance on Rh-based catalysts was reached for a sample containing 5 wt.% of Rh on Al2O3, while Co-based catalysts were suitable only for higher loading of active phase (i.e. 20 wt.%). The supports influence has been also investigated as well as different behavior was been found as a function of their nature. In fact, while Rh (5 wt.%) doped Al2O3 seems to be stable and active catalyst, the Co (20 wt.%)/Al2O3 decays in short time because of coke deposition. The MgO represents a more suitable support for Co catalyst because of its lower acidity with respect to Al2O3 Samples of Co (20 wt.%)/MgO catalysts have been found more stable than Co/Al2O3 (low coke formation) and reached performance levels comparable to that of Rh/Al2O3. Although Co/MgO required higher contact times than Rh/Al2O3, to be used in IIR-MCFCs, it represents an interesting and cheaper alternative to noble metal (Rh). (C) 2001 Elsevier Science B.V. All rights reserved.
引用
收藏
页码:198 / 204
页数:7
相关论文
共 10 条
[1]   Ethanol steam reforming on Rh/Al2O3 catalysts [J].
Cavallaro, S .
ENERGY & FUELS, 2000, 14 (06) :1195-1199
[2]   The influence of oxide-oxide interaction on the catalytic properties of Co/Al2O3 in CO hydrogenation [J].
Chernavskii, PA ;
Pankina, GV ;
Lunin, VV .
CATALYSIS LETTERS, 2000, 66 (03) :121-124
[3]   Ethanol steam reforming in a molten carbonate fuel cell: A thermodynamic approach [J].
Freni, S ;
Maggio, G ;
Cavallaro, S .
JOURNAL OF POWER SOURCES, 1996, 62 (01) :67-73
[4]   Hydrogen production by steam reforming of ethanol: A two step process [J].
Freni, S ;
Mondello, N ;
Cavallaro, S ;
Cacciola, G ;
Parmon, VN ;
Sobyanin, VA .
REACTION KINETICS AND CATALYSIS LETTERS, 2000, 71 (01) :143-152
[5]   HYDROGEN-PRODUCTION BY THE STEAM REFORMING OF ETHANOL - THERMODYNAMIC ANALYSIS [J].
GARCIA, EY ;
LABORDE, MA .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1991, 16 (05) :307-312
[6]   Effect of crystallite size on the catalysis of alumina-supported cobalt catalyst for steam reforming of ethanol [J].
Haga, F ;
Nakajima, T ;
Yamashita, K ;
Mishima, S .
REACTION KINETICS AND CATALYSIS LETTERS, 1998, 63 (02) :253-259
[7]   Catalytic properties of supported cobalt catalysts for steam reforming of ethanol [J].
Haga, F ;
Nakajima, T ;
Miya, H ;
Mishima, S .
CATALYSIS LETTERS, 1997, 48 (3-4) :223-227
[8]  
Rostrup-Nielsen J.R., 1984, CATAL SCI TECHNOL, V5, P1, DOI [DOI 10.1007/978-3-642-93247-2_, DOI 10.1007/978-3-642-93247-2_1]
[9]   Formation of carbon nanotubes from the carbon monoxide disproportionation reaction over Co/Al2O3 and Co/SiO2 catalysts [J].
Thaib, A ;
Martin, GA ;
Pinheiro, P ;
Schouler, MC ;
Gadelle, P .
CATALYSIS LETTERS, 1999, 63 (3-4) :135-141
[10]   Steam reforming of ethanol for hydrogen production: Thermodynamic analysis [J].
Vasudeva, K ;
Mitra, N ;
Umasankar, P ;
Dhingra, SC .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1996, 21 (01) :13-18