Thermodynamic analysis of ethanol/water system with the stoichiometric method

被引:116
作者
Mas, V [1 ]
Kipreos, R [1 ]
Amadeo, N [1 ]
Laborde, M [1 ]
机构
[1] Univ Buenos Aires, Sch Engn, Dept Chem Engn, RA-1428 Buenos Aires, DF, Argentina
关键词
hydrogen; ethanol steam reforming; chemical equilibrium;
D O I
10.1016/j.ijhydene.2005.04.004
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
An analysis of the chemical equilibrium of ethanol/water system, using the stoichiometric method, has been performed. Intermediate compounds and coke formation are analyzed. Ethanol is completely converted to ethylene and/or acetaldehyde. Taking into account the equilibrium constant values of formation and transformation reactions of ethylene and acetaldehyde, both compounds are intermediates in this system. Due to the relevance of carbon monoxide if hydrogen is used as feed of a PEM-type fuel cell, CO concentration in the equilibrium mixture was studied assuming two different scenarios: (a) CO as primary product and (b) CO2 as primary product. These two scenarios lead to suggest different routes for reaching the equilibrium. Thus, the results obtained in this work might help to interpret the experimental results far away from the equilibrium with the aim of elucidating the reaction mechanism. The knowledge of this mechanism is essential in order to minimize the CO formation. The thermodynamic feasibility of coke formation shown in a temperature vs. water/ethanol molar ratio has also been analyzed. The results indicate that if moderate temperatures are used, a molar ratio higher than 3 is required to avoid coke formation. (c) 2005 International Association for Hydrogen Energy. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:21 / 28
页数:8
相关论文
共 22 条
[11]   Synthesis gas production by steam reforming of ethanol [J].
Galvita, VV ;
Semin, GL ;
Belyaev, VD ;
Semikolenov, VA ;
Tsiakaras, P ;
Sobyanin, VA .
APPLIED CATALYSIS A-GENERAL, 2001, 220 (1-2) :123-127
[12]   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
[13]   Thermodynamic analysis of ethanol processors for fuel cell applications [J].
Ioannides, T .
JOURNAL OF POWER SOURCES, 2001, 92 (1-2) :17-25
[14]   REFORMING OF ETHANOL - DEHYDROGENATION TO ETHYL-ACETATE AND STEAM REFORMING TO ACETIC-ACID OVER COPPER-BASED CATALYSTS [J].
IWASA, N ;
TAKEZAWA, N .
BULLETIN OF THE CHEMICAL SOCIETY OF JAPAN, 1991, 64 (09) :2619-2623
[15]  
KIPREOS R, 2003, THESIS U BUENOS AIRE
[16]  
Klouz V., 2001, Journal of Power Sources, V4549, P1
[17]   Light alcohols methane fuelled molten carbonate fuel cells: a comparative study [J].
Maggio, G ;
Freni, S ;
Cavallaro, S .
JOURNAL OF POWER SOURCES, 1998, 74 (01) :17-23
[18]   Hydrogen production from steam reforming of bioethanol using Cu/Ni/K/γ-Al2O3 catalysts.: Effect of Ni [J].
Mariño, F ;
Boveri, M ;
Baronetti, G ;
Laborde, M .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2001, 26 (07) :665-668
[19]  
Marino F., 2002, APPL CATAL A-GEN, V6043, P1
[20]   Hydrogen from steam reforming of ethanol. Characterization and performance of copper-nickel supported catalysts [J].
Marino, FJ ;
Cerrella, EG ;
Duhalde, S ;
Jobbagy, M ;
Laborde, MA .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 1998, 23 (12) :1095-1101