2024 AIChE Annual Meeting
(546c) Multiphase Simulation of Bioreactors to Improve Biofuel Production at Scale
Authors
A Michaelis–Menten kinetic model for the growth and uptake rates of the relevant microorganisms, substrate and other dissolved species, is developed using data from lab-scale stirred tank bioreactors. This model is coupled with a multiphase fluid dynamics model [2,3] and validated using data from the lab-scale bioreactor, then used to estimate the performance of an industrial-scale stirred tank bioreactor. Detailed analysis of the hydrodynamics as well as the substrate concentrations inside this bioreactor enables us to identify the key factors that impact production efficiencies at industrial scale.
References:
[1] https://www.iata.org/en/programs/environment/sustainable-aviation-fuels/
[2] Rahimi, M. J., Sitaraman, H., Humbird, D., and Stickel, J. J. (2018). Computational fluid dynamics study of full-scale aerobic bioreactors: Evaluation of gas–liquid mass transfer, oxygen uptake, and dynamic oxygen distribution. Chemical Engineering Research and Design, 139, 283–295
[3] Sitaraman H, Lischeske J, Stickel J & Lu Y (2023). A reacting multiphase computational flow model for 2,3-butanediol synthesis in industrial-scale bioreactors, Chemical Engineering Research and Design, 197, 2023, 38-52