Mf. Tschantz et al., DEVELOPMENT OF A FULLY SUSPENDED, MULTISTAGE BIOREACTOR SYSTEM FOR TRICHLOROETHYLENE DEGRADATION BASED ON SOLUBLE MONOOXYGENASE COMETABOLISM, Journal of environmental science and health. Part A: Environmental science and engineering, 31(1), 1996, pp. 249-266
The design and operation of a pressurized dual-staged continuous flow
bioreactor for the biodegradation of trichloroethylene (TCE) is presen
ted. The reactor was designed to maximize the utility of the enzyme so
luble methane monooxgenase (sMMO) by the methanotroph, Methylosinus tr
ichosporium, OB3b (PP358), which can produce sMMO even in the presence
of copper. Methane-fed cell growth in a continuous stirred tank react
or (CSTR) was decoupled from TCE oxidation in a methane-free series of
plug-flow columns, minimizing competitive inhibition. The biomass con
centrations were maximized by operating the reactor at 3.04 atm, incre
asing the gas-phase solubility of methane, which increased the growth
rate of the cells. Furthermore, washout of the reactor biomass in the
continuous flow-through system was minimized through the use of a tang
ential now dewatering device. The biodegradative potential of the reac
tor was demonstrated by feeding TCE at concentrations of 0.2 mg/L and
1 mg/L at 2 mL/min. The TCE was completely degraded when TCE was fed a
t 0.2 mg/L and over 95% of the TCE fed at 1 mg/L was degraded. The mea
sured TCE losses were due entirely to biodegradation. Batch abiotic ex
periments showed the reactor held pressure, and losses due to strippin
g and adsorption were minimal over 4 h. The TCE was fed abiotically in
to the reactor at 1 mg/L, and 92 h of operation was necessary for the
reactor TCE concentrations to accumulate to that of the feed. The abio
tic mass balances demonstrated that in the absence of biodegradation,
the reactor TCE concentrations would accumulate to that of the feed. T
he ability to close mass balances, coupled with the ability to closely
control and monitor reactor conditions, allows for a system that may
be utilized to construct a mechanistic model describing the kinetics o
f TCE degradation by sMMO and may potentially maxi mite the ut iii ty
of the methanotrophs for TCE biodegradation at high feed concentration
s.