Biotechnology and Bioengineering · 1991 · 81 citations · 36 references
Life SciencesBiotechnologyMicrobiologyBiocatalysisBiochemical EngineeringBioprocess EngineeringBioprocess KineticsBioprocess ModelingBioreaction EngineeringEnzyme ImmobilizationMicrobial BiocatalysisMicrobial GrowthAirlift ReactorsBiocatalyst ImmobilizationBiomass Growth KineticsBioreactor KineticsMass Transfer KineticsMass Transfer MechanismsOxygen Consumption KineticsOxygen Utilization Rate
The modeling of the growth of Nitrobacter agilis cell immobilized in kappa-carrageenan is presented. A detailed description is given of the modeling of internal diffusion and growth of cells in the support matrix in addition to external mass transfer resistance. The model predicts the substrate and biomass profiles in the support as well as the macroscopic oxygen consumption rate of the immobilized biocatalyst in time. The model is tested by experiments with continuously operated airlift loop reactors containing cells immobilized in kappa-carrageenan. The model describes experimental data very well. It is clearly shown that external mass transfer may not be neglected. Furthermore, a sensitivity analysis of the parameters at their values during the experiments revealed that apart from the radius of the spheres and the substrate bulk concentration, the external mass transfer resistance coefficient is the most sensitive parameter for our case.
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Design parameters estimations for bubble column reactors
Y. T. Shah, B.G. Kelkar, S. P. Godbole et al. · AIChE Journal · 1982 · 1.2K citations
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Recent Progress in Microbiology
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