To assess the technical feasibility and economic potential of such a process, it is conceptually designed on a 100,000 t/a scale. Due to the poor solubility of CO and H2 in water, it is assumed that the mass transfer in the fermentor will be the major process rate limiting factor [Munasinghe and Khanal (2010) Bioresour. Technol. 101, 5013]. Estimates show that mega-fermentor sizes are required when using stirred tanks. Alternative bioreactors are designed. One extra degree of freedom is obtained when combining fermentation with the water-gas shift reaction before fermentation step, in order to manipulate the CO/H2 ratio in the fermentation inlet gas. Another option considered is to use thermophilic organisms at high temperature process to transfer ethanol to the gas phase during the fermentation. This facilitates cell retention and reduces downstream processing costs.
Initial estimates show that the lowest capital investments are obtained when using H2-rich syngas.