The rate of oxygen transfer from
the gas phase to the liquid phase
is a critical process parameter for biocatalytic oxidations due to
the poor water solubility of molecular oxygen and the low oxygen affinity
of many of the relevant enzymes, such as oxidases. In gas–liquid
systems, mechanical mixing can be used to increase the interfacial
area available for mass transfer and thereby increase the volumetric
mass transfer coefficient (k
L
a). As such, the operation of these reactions in a continuous stirred
tank reactor (CSTR) may allow for better performance in a readily
scalable way. Even so, achieving a high substrate conversion in a
single reactor would require operation at high pressure, to improve
the solubility of oxygen, as well as a high enzyme concentration.
An alternative and more cost-effective means of improving the substrate
conversion might be to operate a series of multiple CSTRs. As such,
the oxidation of glucose to gluconic acid by glucose oxidase, coupled
with catalase, was modeled in a series of identical well-mixed reactors.
It was found that achieving full conversion would require an impractical
number of reactors at atmospheric pressure. However, the overall conversion
of the reaction could be doubled by simply using two CSTRs in series.
Subsequently, experiments were carried out to validate this, and the
results showed that the overall conversion was in fact tripled. This
likely resulted from a higher k
L
a in the second reactor, which was potentially caused by
the change in the media composition from the first reactor.