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Biotransformation of cephalosporin C to 7-aminocephalosporanic acid with coimmobilized biocatalyst in a batch bioreactor
Authors:P. Ačai  E. Michálková  V. Báleš
Affiliation:(1) Faculty of Chemical Technology, Department of Chemical and Biochemical Engineering, Slovak Technical University, Radlinského 9, 812 37 Bratislava, Slovakia;(2) Biotika Co., Slovenská L'up"ccaron"a, 976 13 Slovenská L'up"ccaron"a, Slovakia;(3) Faculty of Chemical Technology, Department of Chemical and Biochemical Engineering, Slovak Technical University, Radlinského 9, 812 37 Bratislava, Slovakia
Abstract:Biotransformation of cephalosporin C (CPS-C) to 7-aminocephalosporanic acid (7-ACA) was carried out with coimmobilized permeabilized cells of Trigonopsis variabilis and Pseudomonas species entrapped in Ca-pectate gel beads. Good aeration and stirring during the process was assured. The analysis of this complicated biochemical process in a heterogeneous system was based on the identification of individual effects (internal diffusion, reaction) running simultaneously. A spectrophotometric method was proposed for the determination of 7-(agr-ketoadipyl amido) cephalosporanic acid (CO-GL-7-ACA) and 7-ACA. The reaction-diffusion model containing dimensionless partial differential equations was solved by using the orthogonal collocation method. A good agreement between experimental values and values predicted by the mathematical model was obtained. Numerical simulations were performed on the basis of following the two assumptions:- several times higher activity of both cells,- hydrogen peroxide was continuously supplied in the bioreactor.List of Symbols A m2 surface of the bead - cimol/dm3 concentration of component in the bead and/or in the solution - ci0mol/dm3 initial concentration of component in the solution - cl0mol/dm3 initial concentration of CPS-C in the solution - Cjl orthogonal collocation weights of the first derivation - Deim2/s effective diffusion coefficient of the components - Djl orthogonal collocation weights of the second derivation - k5 dm3/(mol · s) kinetic parameter of non-enzyme reaction - Kinhmol/dm3 inhibition parameter for the first enzyme reaction - Ki dimensionless Michaelis constant for the first and second enzyme reaction, defined in Eq. (7) - Kl dimensionless inhibition parameter for the first enzyme reaction, defined in Eq. (7) - Kmimol/dm3 Michaelis constant for the first and second enzyme reaction - n number of beads - P(gammai) symbol of dimensionless reaction rate, defined in Eq. (13) - r m radial coordinate inside the bead - R m radius of the bead - R(ci) mol/(dm3 · s) symbol for reaction rate, defined in Eq. (6) - t s time - Vmax mol/(dm3 · s) max. reaction rate for the first and second enzyme reaction - VLdm3 volume of solution excluding the space occupied by beads - epsiv voidage in batch bioreactor - epsivP porosity of the bead - Deltai dimensionless effective diffusion coefficient of the components, defined in Eq. (7) - tau dimensionless time, defined in Eq. (7) - PHgrmi Thiele modulus, defined in Eq. (7) - gammai dimensionless concentration, defined in Eq. (7) - rgr dimensionless radial position inside the bead, defined in Eq. (7) - gammal0 initial dimension concentration of CPS-C, defined in Eq. (9), (10) - gammai0 initial dimension concentration of component, defined in Eq. (9), (10)The authors wish to thank Dr. P. Gemeiner of Slovak Academy of Sciences for rendering of pectate gel. This work is supported by Ministry of Education (Grant No. 1/990 935/93).
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