Mathematical modeling of ethanol production by immobilized Zymomonas mobilis in a packed bed fermenter
Michael R. Melick, M. Nazmul Karim, James C. Linden, Bruce E. Dale, P. Miháltz
Abstract
Michael R. Melick, M. Nazmul Karim, James C. Linden, Bruce E. Dale, P. Miháltz
Abstract
A mathematical model which describes ethanol production in a packed bed fermenter containing. Zymomonas mobilis entrapped in small spheres of calcium alginate within a packed bed fermenter has been developed. The equations combine simultaneous diffusion and reaction as well as a complex flow pattern to calculate glucose and ethanol profiles in the column type reactor. As part of the study, diffusivity values for glucose and ethanol in cell-loaded calcium alginate were determined. Also a freecell kinetic expression for Z. mobilis at 33 degrees C and ph 6.0 was developed. Comparison of the model with actual experimental results were made showing average deviations of ca. 30-40%.
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A mathematical model which describes ethanol production in a packed bed fermenter containing. Zymomonas mobilis entrapped in small spheres of calcium alginate within a packed bed fermenter has been developed. The equations combine simultaneous diffusion and reaction as well as a complex flow pattern to calculate glucose and ethanol profiles in the column type reactor. As part of the study, diffusivity values for glucose and ethanol in cell-loaded calcium alginate were determined. Also a freecell kinetic expression for Z. mobilis at 33 degrees C and ph 6.0 was developed. Comparison of the model with actual experimental results were made showing average deviations of ca. 30-40%.
Key concepts: Zymomonas mobilis, Industrial fermentation, Calcium alginate, Packed bed, Chemistry, Ethanol, Ethanol fuel, Thermal diffusivity