In this work a novel coal fueled power plant, which combines coal gasi
fication and solid oxide fuel cell technology, is presented. The cycle
is a modification of an earlier one proposed by the same authors [Lob
achyov and Richter, Journal of Energy Resources Technology, 1996, 188]
. It retains most of the elements of the previous plant: Conoco CO2 ac
ceptor gasification process, solid oxide fuel cell and state-of-the-ar
t gas turbines. A key difference between the previous and the new cycl
e is a different heat recovery concept. Instead of using the sensible
heat of the cathode exhaust for the coal gasification process, the fue
l not oxidized in the fuel cell is burnt to provide this heat. This ne
w concept allows us to simplify the cycle and makes its performance le
ss dependent on the pressure drop in different components of the cycle
. Further, it considerably reduces the exergy loss in the gas turbine
by eliminating exergetically inefficient turbine blade cooling. The ne
w cycle achieves a gain in the overall efficiency of more than two per
centage points under the same operating parameters. At a maximum syste
m pressure of 10 bar and an anticipated solid oxide fuel cell voltage
of 0.7 V the overall thermal efficiency is approximately 63%. (C) 1997
Elsevier Science Ltd.