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Experimental Study of Biodegradation of Ethanol and Toluene Vapors

Experimental Study of Biodegradation of Ethanol and Toluene Vapors

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When the concept <strong>of</strong> inhibited co-metabolism is applied to bioremediation <strong>of</strong><br />

mixtures <strong>of</strong> toluene <strong>and</strong> ethanol, it is assumed that biomass formed from ethanol <strong>and</strong><br />

toluene acts as an inhibitor (Bailey <strong>and</strong> Ollis, 1986; Chang et al, 1993; Bielefeldt <strong>and</strong><br />

Stensel, 1999). In addition to the reaction Equations (5-3), (5-10) <strong>and</strong> (5-11) for ethanol<br />

bioremediation, toluene catabolism is represented by Equation (5-44) on a 1 C-mol<br />

basis, which was derived from the toluene pathway (Davey <strong>and</strong> Gibson, 1974; Wackett,<br />

2004, see Appendix A-III):<br />

CH<br />

8 / 7<br />

8 3 12<br />

r 12<br />

+ H<br />

2O<br />

+ O2<br />

+ NAD ⎯⎯→<br />

4 NADH<br />

2<br />

+<br />

2<br />

7 7 7<br />

7<br />

CO<br />

(5-44)<br />

The stoichiometric matrix, θ<br />

et , for four reactions (5-3), (5-10), (5-11) <strong>and</strong> (5-44) can be<br />

written as<br />

r e<br />

r t<br />

r x<br />

-1.27 -1 0 0<br />

0 0 0 -1<br />

1 0 0 0<br />

3<br />

θ<br />

et = r o2<br />

= 0 0 -0.5 − (5-45)<br />

7<br />

0.27 1 0 1<br />

r co2<br />

rATP<br />

-α1E -0.5 δ 0<br />

12<br />

r<br />

NADH<br />

1.81 3 -1<br />

7<br />

The reaction rate vector ν for four reactions (5-3), (5-10), (5-11), <strong>and</strong> (5-44) can be<br />

written as:<br />

ν 1<br />

ν r = ν 2 (5-46)<br />

ν 3<br />

ν 4<br />

112

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