Bioreactor scale-up and oxygen transfer rate in microbial processes: an overview.
By F. García-Ochoa, E. Gómez. Biotechnology Advances, 2009
1,439 citations recorded by the source corpus.
Subfields: Biomedical Engineering, Water Science and Technology
View Paper: https://www.semanticscholar.org/paper/478df952de998862bdf0580741508b17a5f19106
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In Biomedical Engineering
In Water Science and Technology
Citations in the corpus
- Process Design and Economics for the Conversion of Lignocellulosic Biomass to Hydrocarbons: Dilute-Acid and Enzymatic Deconstruction of Biomass to Sugars and Biological Conversion of Sugars to Hydrocarbons (2013, background): “Molecular oxygen (O2) has low solubility in aqueous media and the solubility also decreases with elevated temperature and increases in broth osmolarity and viscosity [44].”
- Oxygen uptake rate in microbial processes: An overview (2010, methodology): “[40] V.E. Santos, C. Galdeano, E. Gomez, A. Alcon, F. Garcia-Ochoa, Oxygen uptake rate measurements both by the dynamic method and during the process growth of Rhodococcus erythropolis IGTS8: modelling and difference in results, Biochem.”
- Impact of rheology on the mass transfer coefficient during the growth phase of Trichoderma reesei in stirred bioreactors (2012, background): “In the past, many correlations have been proposed to predict the kla in stirred reactors with complex fluids (Nishikawa et al., 1981; Kawase and Mooyoung, 1988; Garcia-Ochoa and Gomez, 2009; Cooke et al., 1988).”