a the solid oxide fuel cell (SOFC) system, the internal reforming of raw fu
el will act as an efficient cooling system. To realize this cooling system,
a special design of the internal reformer is required to avoid the inhomog
eneous temperature distribution caused by the strong endothermic reforming
reaction at the entrance of the internal reformer. For this purpose, a tubu
lar internal reformer with adjusted catalyst density can be inserted into t
he tubular SOFC stack. By arranging this, the raw fuel flows along the axis
of the internal reformer to be moderately reformed and returns at the end
of the internal reformer as a sufficiently reformed fuel.
In this paper, the output characteristics of this configuration are simulat
ed using mathematical models, in which one-dimensional temperature and mola
r distributions are computed along the flow direction. By properly mounting
the catalyst density in the internal reformer, the temperature distributio
n of the cell stack becomes moderate, and the power generation efficiency a
nd the exhaust gas temperature are higher. Effects of other operating condi
tions such as fuel recirculation, fuel inlet temperature, air recirculation
and air inlet temperature are also examined under the condition where the
maximum temperature of the stack is kept at 1300 K by adjusting the air flo
w rate. Under this condition, these operating conditions exert a considerab
le effect on the exhaust temperature but have a slight effect on the effici
ency. (C) 2001 Elsevier Science B.V. All rights reserved.