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Abstract
Chemically recuperated Gas Turbine (CRGT) that recovers exhaust heat by endothermic reaction converting fuel to reforming gas is one of candidates for effective utilization of ethanol from biomass fermentation. Bio-ethanol can easily be applied to steam reforming process for hydrogenrich gas production, because the moisture in bio-ethanol is included about 80% after the fermentation process. The chemical composition in reformer was evaluated according to chemical equilibrium equations. This numerical analysis reports a performance comparison with simple cycle gas turbine. Thermochemical recuperation in the ethanol was allowed to achieve a significant change in power output, and the maximum increase in thermal efficiency was 16% compared with simple cycle at 8.0 in steam/fuel molar ratio and 600 deg. C in reforming temperature.
Journal
- Transactions of the Japan Society of Mechanical Engineers. B [List of Volumes]
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Transactions of the Japan Society of Mechanical Engineers. B 73(730), 1331-1336, 2007-06-25 [Table of Contents]
The Japan Society of Mechanical Engineers