A numerical study was conducted to analyse the e!ect of #ow distribution of stirred part and plug #ow part on combustion e$ciency at the coal gasi"cation process in an entrained bed coal reactor. The model of computation was based on gas-phase Eulerian balance equations of momentum and mass. The sol
Effect of enzyme inhibition on the performance of packed-bed biological reactor - a theoretical study
โ Scribed by M. M. Hassan; Prof. Dr. S. A. Beg
- Publisher
- John Wiley and Sons
- Year
- 1988
- Tongue
- English
- Weight
- 448 KB
- Volume
- 11
- Category
- Article
- ISSN
- 0930-7516
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โฆ Synopsis
The performance characteristic of a packed bed reactor has been analyzed by considering diffusional resitance of the biofilm. Model equations were solved by the method of orthogonal collocation for various classical enzyme inhibition kinetics, including partially non-competitive, partially competitive, partially uncompetitive, partially mixed and fully mixed. For all considered modes of inhibition, an increase in the inlet substrate concentration decreases the steady state conversion in the reactor. However, an increase in the Peclet number has been found to improve the conversion. The effects of various other process variables of physical importance were also investigated parametrically.
๐ SIMILAR VOLUMES
## Abstract The performance of an immobilized packed bed reactor for the hydrolysis of rice bran oil has been investigated and can be well described by a dispersion model with an average standard deviation of 0.0388. Global mass transfer coefficients estimated using the model and experimental data