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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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Appendix D: Mathematical Solutions <strong>and</strong> Derivations<br />

Appendix D-1. Model for <strong>Ethanol</strong> Bioremediation<br />

For ethanol bioremediation, the overall conversion rates <strong>of</strong> the key compounds<br />

are given in Section 5.1.2 as:<br />

r = −1.27ν −ν<br />

(5-14a)<br />

e<br />

1<br />

2<br />

r<br />

x<br />

=ν 1<br />

(5-14b)<br />

r (5-14c)<br />

o<br />

= −0.5ν<br />

2 3<br />

co<br />

= 0.27ν 2 1<br />

+ ν<br />

2<br />

r (5-14d)<br />

− α E<br />

⋅ν<br />

− .5 ⋅ν<br />

+ δ ⋅ν<br />

0<br />

(5-14e)<br />

1 1<br />

0<br />

2 3<br />

=<br />

.81⋅ν + 3ν<br />

−ν<br />

0<br />

(5-14f)<br />

1<br />

1 2 3<br />

=<br />

From the above equations it is possible to express the overall conversion rates <strong>of</strong><br />

ethanol, oxygen, <strong>and</strong> carbon dioxide, in terms <strong>of</strong><br />

r x<br />

(overall conversion rate <strong>of</strong> biomass).<br />

Solving Equations (5-14f) <strong>and</strong> (5-14g) simultaneously, the reaction rates for the second<br />

<strong>and</strong> third reactions, ν<br />

2<br />

<strong>and</strong>ν 3<br />

, can be expressed as a function <strong>of</strong> the biomass synthesis<br />

rate (r x = ν 1<br />

) as shown in Equation (D-1):<br />

ν<br />

2<br />

( α1E<br />

−1.81δ<br />

)<br />

=<br />

⋅ν<br />

1<br />

(3δ<br />

− 0.5)<br />

(D-1)<br />

Considering Equation (5-4): α<br />

1 E<br />

mATP<br />

= K +<br />

μ<br />

ν<br />

3<br />

=<br />

ν +<br />

(3α<br />

− 0.905)<br />

ν =<br />

⋅ν<br />

(3δ<br />

− 0.5)<br />

1E<br />

1.81<br />

1<br />

3<br />

2<br />

1<br />

mATP<br />

3( K + ) − 0.905<br />

μ<br />

= {<br />

} ⋅ r<br />

3δ<br />

− 0.5<br />

x<br />

(D-2)<br />

185

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