In the present study, a detailed thermodynamic analysis has been carried ou
t in order to provide useful information concerning ethanol utilization as
alternative fuel in solid oxide fuel cells (SOFCs). by using different oxid
ants for preliminary fuel reforming. The SOFC was considered being fed with
the thermodynamic equilibrium products of ethanol, (a) steam reforming, (b
) reforming with CO2 and (c) partial oxidation with air. Equilibrium calcul
ations were performed in the region where carbon formation is thermodynamic
ally impossible, in the temperature range between 800, and 1200 K assuming
different oxidant/ethanol ratios of the initial system.
It was found that the maximum SOFC system efficiency at T < 950 and > 1100
K is achieved when the SOFC electrochemical section is fed by the products
of ethanol steam reforming, whereas at the intermediate temperature region
it seems more preferable to feed the SOFC electrochemical section with the
products of ethanol reforming with carbon dioxide. Maximum obtainable SOFC
system efficiency if the products of ethanol partial oxidation feed the SOF
C electrochemical section is about 20% less compared to the maximum SOFC sy
stem efficiency in the previous cases. (C) 2001 Elsevier Science B.V. All r
ights reserved.