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- 2009 Annual Meeting
- Fuels and Petrochemicals Division
- Alternative Fuels and Enabling Technology II
- (238b) Modeling and Optimization of Fischer-Tropsch Synthesis Processes
The gas-phase model is used as the foundation for a model of the supercritical phase Fischer-Tropsch Synthesis (SCF-FTS) process being developed at Auburn University. By operating the FTS reaction in a dense phase, the direct benefits are two-fold, i.e. vapor-like transport properties and liquid-like thermal properties. This means that the product distribution is much more narrow than traditional gas-phase FTS. Using experimental data generated within CFFS, models have also been developed for analysis of the supercritical water reforming (SCWR) for hydrogen production from biomass. The high-pressure hydrogen produced from supercritical water reforming is intended for injection in the SCF-FTS process during the cracking/isomerization step.
Economic and environmental analysis was performed through quantifying the level of environmental impact using EPA's WAR algorithm. In this way, experimental and theoretical efforts can supplement each other, providing direction for further research.