Heterogeneous one-dimensional model for fixed bed enzyme reactors
- 1 August 1986
- journal article
- research article
- Published by Wiley in Biotechnology & Bioengineering
- Vol. 28 (8) , 1256-1260
- https://doi.org/10.1002/bit.260280818
Abstract
A one-dimensional model, taking into account the diffusion of substrate between the liquid phase and the solid support, has been used to describe fixed bed enzyme reactors. The equations were solved numerically, and the values of the different parameters were calculated by a nonlinear regression method. The model was applied to different systems. The results are presented and discussed.This publication has 17 references indexed in Scilit:
- Enzyme immobilized in a packed-bed reactor: Kinetic parameters and mass transfer effectsBiotechnology & Bioengineering, 1975
- Film diffusion and Michaelis-Menten kinetics in a packed-bed reactorBiotechnology & Bioengineering, 1975
- Effects of internal diffusion on the lineweaver‐Burk plots for immobilized enzymesBiotechnology & Bioengineering, 1975
- Influence of intraparticle diffuisional limitation on the observed kinetics of immobilized enzymes and on catalyst designBiotechnology & Bioengineering, 1974
- Effectiveness factor calculations for immobilized enzyme catalystsBiotechnology & Bioengineering, 1973
- Film and pore diffusion studies with immobilized glucose oxidaseBiotechnology & Bioengineering, 1973
- Effectiveness factors for immobilized‐enzyme reactionsThe Canadian Journal of Chemical Engineering, 1972
- Backmixing and mass transfer in the design of immobilized‐enzyme reactorsBiotechnology & Bioengineering, 1971
- The kinetics of carboxymethylcellulose–ficin in packed bedsBiochemical Journal, 1966
- Continuous flow systemsChemical Engineering Science, 1953