Abstract
An integrated gasification solid oxide fuel cell (SOFC) and Stirling engine for combined heat and power
application is analyzed. The target for electricity production is 120 kW. Woodchips are used as gasification
feedstock to produce syngas, which is then used to feed the SOFC stacks for electricity production.
Unreacted hydrocarbons remaining after the SOFC are burned in a catalytic burner, and the hot off-gases
from the burner are recovered in a Stirling engine for electricity and heat production. Domestic hot water
is used as a heat sink for the Stirling engine. A complete balance-of-plant is designed and suggested.
Thermodynamic analysis shows that a thermal efficiency of 42.4% based on the lower heating value
(LHV) can be achieved if all input parameters are selected conservatively. Different parameter studies are
performed to analyze the system behavior under different conditions. The analysis shows that the
decreasing number of stacks from a design viewpoint, indicating that plant efficiency decreases but
power production remains nearly unchanged. Furthermore, the analysis shows that there is an optimum
value for the utilization factor of the SOFC for the suggested plant design with the suggested input
parameters. This optimum value is approximately 65%, which is a rather modest value for SOFC. In
addition, introducing a methanator increases plant efficiency slightly. If SOFC operating temperature
decreases due to new technology then plant efficiency will slightly be increased. Decreasing gasifier
temperature, which cannot be controlled, causes the plant efficiency to increase also.
© 2014 Elsevier Ltd. All rights reserved.
Original language | English |
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Journal | Energy |
Volume | 77 |
Pages (from-to) | 6-18 |
ISSN | 0360-5442 |
DOIs | |
Publication status | Published - 2014 |
Keywords
- SOFC
- Fuel cell
- Hybrid cycle
- Stirling engine
- Gasification