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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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1<br />

max<br />

Y ex<br />

=<br />

− 0.635 + 2δ<br />

+ K<br />

3δ<br />

− 0.5<br />

(5-15a)<br />

matp<br />

m<br />

e<br />

= (5-15b)<br />

3 δ − 0.5<br />

Equations (5-15a) <strong>and</strong> (5-15b) provide relations between the three energetic<br />

parameters: K ,δ , m . If we assume that these three parameters are fundamental<br />

ATP<br />

parameters for the strain, then a similar model as derived above can be derived for other<br />

substrates, <strong>and</strong> in this model the yield coefficients will be different functions <strong>of</strong> the<br />

three energetic parameters. If the yield coefficients are experimentally determined for<br />

growth on different substrates the energetic parameters can be estimated (Nielsen <strong>and</strong><br />

Villadsen, 2001). An important assumption in this approach is that the values <strong>of</strong><br />

parameters do not change with the carbon source, even though the functions change<br />

with different carbon sources.<br />

For continuous operation, at steady state, r = 0 , thus the following equations<br />

can be obtained from Equation (5-14):<br />

r r<br />

φ = −θ<br />

e<br />

⋅ν<br />

(5-16)<br />

φ<br />

e<br />

= 1.27ν<br />

+ ν<br />

(5-16a)<br />

1<br />

2<br />

φx = −ν 1<br />

(5-16b)<br />

where<br />

φ<br />

e<br />

<strong>and</strong> φ x<br />

are the flow <strong>of</strong> ethanol <strong>and</strong> biomass into the system (C-mol/L-h),<br />

respectively. Therefore, by coupling Equations (5-14e), (5-14f) with Equations (5-16a)<br />

<strong>and</strong> (5-16b), the relation between the flows <strong>of</strong> ethanol <strong>and</strong> biomass at steady state in<br />

continuous mode can be expressed by (see Appendix D for detailed mathematical<br />

derivations):<br />

87

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