Characterization of a continuous agitated cell reactor for oxygen dependent biocatalysis. Issue 6 (23rd February 2017)

• Record Type: Journal Article
• Authors: Toftgaard Pedersen, Asbjørn; de Carvalho, Teresa Melo; Sutherland, Euan; Rehn, Gustav; Ashe, Robert; Woodley, John M.
• Is Part Of: Biotechnology and bioengineering. Volume 114:Issue 6(2017)
• Page Start: 1222
• Page End: 1230
• Publication Date: 2017-02-23
• Subjects: continuous biocatalysis -- gas‐liquid mixing -- glucose oxidase -- hydrodynamics -- oxygen transfer rate; Biotechnology -- Periodicals; Bioengineering -- Periodicals; 660.6
• DOI: 10.1002/bit.26267
• Languages: English
• ISSNs: 0006-3592

Abstract

ABSTRACT: Biocatalytic oxidation reactions employing molecular oxygen as the electron acceptor are difficult to conduct in a continuous flow reactor because of the requirement for high oxygen transfer rates. In this paper, the oxidation of glucose to glucono‐1, 5‐lactone by glucose oxidase was used as a model reaction to study a novel continuous agitated cell reactor (ACR). The ACR consists of ten cells interconnected by small channels. An agitator is placed in each cell, which mixes the content of the cell when the reactor body is shaken by lateral movement. Based on tracer experiments, a hydrodynamic model for the ACR was developed. The model consisted of ten tanks‐in‐series with back‐mixing occurring within and between each cell. The back‐mixing was a necessary addition to the model in order to explain the observed phenomenon that the ACR behaved as two continuous stirred tank reactors (CSTRs) at low flow rates, while it at high flow rates behaved as the expected ten CSTRs in series. The performance of the ACR was evaluated by comparing the steady state conversion at varying residence times with the conversion observed in a stirred batch reactor of comparable size. It was found that the ACR could more than double the overall reaction rate, which was solely due to an increased oxygen transfer rate in the ACR caused by the intense mixing as a result of the spring agitators. The volumetric oxygen transfer coefficient, kL a, was estimated to be 344 h −1 in the 100 mL ACR, opposed to only 104 h −1 in a batch reactor of comparable working volume. Interestingly, the large deviation from plug flow behavior seen in the tracer experiments was found to have little influence on the conversion in the ACR, since both a plug flow reactor (PFR) model and the backflow cell model described the data sufficiently well. Biotechnol. Bioeng. 2017;114: 1222–1230. © 2017 Wiley Periodicals, Inc. Abstract : Continuous biocatalytic oxidation in an agitated cell reactor (ACR) was investigated by applying the oxidation of glucose to glucono‐1, 5‐lactone catalyzed by glucose oxidase as a model reaction. Mathematical models describing the hydrodynamics of the ACR, the mass transfer of oxygen in the ACR, and the kinetics of the enzyme reaction were developed and combined to describe the rate of glucose conversion observed experimentally. Overall, it was shown that the ACR could transfer oxygen significantly faster than a comparable batch reactor.