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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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The continuous models can capture all significant physical phenomena since<br />

they were derived based on fundamental biochemical principles <strong>and</strong> mass balances.<br />

Equations (5-65), (5-69), (5-71), <strong>and</strong> (5-73) illustrate that biomass concentrations are a<br />

function <strong>of</strong> the operating conditions such as inlet <strong>and</strong> outlet concentrations in liquid <strong>and</strong><br />

gas phases, dilution rates, yield coefficients on each substrate, <strong>and</strong> the maintenance<br />

terms under different conditions. If the operating conditions change, the model reflects<br />

the physical reality <strong>of</strong> this change. For instance, for continuous removal <strong>of</strong> ethanol at<br />

steady state conditions, biomass concentration increases as the amount <strong>of</strong> ethanol<br />

introduced from gas phase increases when other conditions remain the same (see<br />

Figures 5-14a <strong>and</strong> 5-14b). For example, results in Figure 5-7 show that the steady state<br />

continuous model predicts the changes in biomass concentrations due to the increase <strong>of</strong><br />

ethanol gas inlet concentration. However, there was not sufficient time to generate more<br />

data to determine the predictive ability <strong>of</strong> the model.<br />

The limitation <strong>of</strong> the simulation is the parameters obtained from the limited (but<br />

time consuming) number <strong>of</strong> experiments such as m, Y m . As discussed in Section 5.4.2,<br />

this maintenance term <strong>of</strong> growth depends on the growth environment such as the type <strong>of</strong><br />

substrate <strong>and</strong> its concentration, operating mode (batch or continuous), <strong>and</strong> conditions <strong>of</strong><br />

other nutrients such as pH, oxygen <strong>and</strong> ammonia. Moreover, in reality the P/O ratio (δ )<br />

may also vary with the operating conditions. Therefore, it is recommended that more<br />

detailed on-line measurements, including ATP, oxygen <strong>and</strong> carbon dioxide, be carried<br />

out in order to verify <strong>and</strong> improve the model in the future.<br />

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