V. Hecht et al., COMETABOLIC DEGRADATION OF TRICHLOROETHYLENE IN A BUBBLE-COLUMN BIOSCRUBBER, Biotechnology and bioengineering, 47(4), 1995, pp. 461-469
A bubble column bioreactor was used as bioscrubber to carry out a feas
ibility study for the cometabolic degradation of trichloroethylene (TC
E). Phenol was used as cosubstrate and inducer. The bioreactor was ope
rated like a conventional chemostat with regard to the cosubstrate and
low dilution rates were used to minimize the liquid outflow, TCE degr
adation measurements were carried out using superficial gas velocities
between 0.47 and 4.07 cm s(-1) and TCE gas phase loads between 0.07 a
nd 0.40 mg L(-1). Depending on the superficial gas velocity used, degr
ees of conversion between 30% and 80% were obtained, A simplified reac
tor model using plug flow for the gas phase, mixed flow for the liquid
phase, and pseudo first order reaction kinetics for the conversion of
TCE was established. The model is able to give a reasonable approxima
tion of the experimental data. ICE degradation at the used experimenta
l conditions is mainly limited by reaction rate rather than by mass tr
ansfer rate. The model can be used to calculate the reactor volume and
the biomass concentration for a required conversion. (C) 1995 John Wi
ley and Sons, Inc.