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Kinetic modeling of xylonic acid production by Gluconobacter oxydans: effects of hydrodynamic conditions

机译:Kinetic modeling of xylonic acid production by Gluconobacter oxydans: effects of hydrodynamic conditions

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Abstract In this study, the synthesis of xylonic acid from xylose by Gluconobacter oxydans NL71 has been investigated. According to the relationship between oxygen transfer rate and oxygen uptake rate, three different kinetic models of product formation were established and the nonlinear fitting was carried out. The results showed that G. oxydans has critical dissolved oxygen under different strain concentrations, and the relationship between respiration intensity and dissolved oxygen conformed to the Monod equation qO2=qO2,maxCLKO2+CLdocumentclass12pt{minimal} usepackage{amsmath} usepackage{wasysym} usepackage{amsfonts} usepackage{amssymb} usepackage{amsbsy} usepackage{mathrsfs} usepackage{upgreek} setlength{oddsidemargin}{-69pt} begin{document}$$q_{{{text{O}}_{2} }} = q_{{{text{O}}_{2} ,max }} frac{{C_{{text{L}}} }}{{K_{{{text{O}}_{2} }} + C_{{text{L}}} }}$$end{document}. The maximum reaction rate per unit cell mass and the theoretical maximum specific productivity of G. oxydans obtained by the kinetic model are 0.042?mol/L/h and 6.97?g/gx/h, respectively. These results will assist in determining the best balance between the airflow rate and cell concentration in the reaction and improve the production efficiency of xylonic acid.

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