Biotechnol Bioeng. 1992 Nov;40(9):1097-106. doi: 10.1002/bit.260400914.

Influence of oxygen adsorption on the dynamic K(L)a measurement in three-phase slurry reactors.

Biotechnology and bioengineering

M Boon, T A Meeder, J J Heijnen, K C Luyben

PMID: 18601219 DOI: 10.1002/bit.260400914

Abstract

To check for possible mass transfer limitations of oxygen and/or carbon dioxide in kinetic experiments on microbial desulphurization of coal, it is important to properly measure the volumetric mass transfer coefficient (k(L)a) especially at high slurry densities. Volumetric mass transfer coefficients of oxygen, at different solid hold-up values (epsilon(s) = 0 to 0.28) of coal slurries (d(par) < 100 * 10(-6) m), were measured in a lab scale fermentor and in a lab scale pachuca tank, using the dynamic gas-liquid absorption method. It was shown that serious errors could occur due to oxygen adsorption at the coal surface. Using the data of an independently measured adsorption isotherm, the real k(L)a could be calculated from the measured apparent k(L)a. The results show a k(L)a decrease of 40% to 50% at a volumetric solid hold-up of 28%. Estimation of the oxygen and carbon dioxide transfer rates, from the measured mass transfer coefficients, indicates that the stirred fermentor is suitable for kinetic experiments at high slurry densities, whereas the pachuca tank and shake flask are not.

(c) 1992 John Wiley & Sons, Inc.

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• Journal Article