Design of a large-scale surface-aerated bioreactor for biomass production using a VOC substrate.
The design of a large-scale bioreactor for the production of bacterial biomass adapted to the biodegradation of volatile organic compounds was carried out. The bioreactor model used integrated the microbial kinetics and fluid dynamics described by the compartment model approach. The process conditions and kinetic parameters were adopted from the laboratory experimental study of (León, E., Seignez, C., Adler, N., Péringer, P., 1999. Growth inhibition of biomass adapted to the degradation of toluene and xylenes in mixture in a batch reactor with substrates supplied by pulses. Biodegradation 10, 245-250). The performance of the pulsed-batch stirred bioreactor under surface aeration conditions was simulated for different mixing configurations and conditions such as the impeller diameter, number of impellers, stirring speed, and oxygen pressure. The simulations were used for the cost analysis which resulted in the optimal design of the bioreactor.
Acai
P
P
Department of Chemical and Biochemical Engineering, Institute of Chemical and Environmental Engineering, Faculty of Chemical and Food Technology, Slovak University of Technology, Radlinského 9, 812 37 Bratislava, Slovak Republic.
Polakovic
M
M
D001673:Biodegradation, Environmental; D018533:Biomass; D019149:Bioreactors; D008954:Models, Biological; D009930:Organic Chemicals / Q000378:metabolism*; D014050:Toluene / Q000378:metabolism; D014835:Volatilization
D009930:Organic Chemicals; D014050:Toluene