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Modeling of Biogas Reactors

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180 6 <strong>Modeling</strong> <strong>of</strong> <strong>Biogas</strong> <strong>Reactors</strong><br />

usual range <strong>of</strong> substrate concentrations. If the system was heavily overloaded for<br />

some time and was out <strong>of</strong> the described range, the microbial population might need<br />

some recovering time, which cannot be described by Eq. 18. Figure 6.16 shows a<br />

sketch <strong>of</strong> different configurations in which active microorganisms exist in biogas reactors.<br />

They can exist in a freely dispersed form, i.e., as single organisms, or as in the<br />

biogas tower reactor in the form <strong>of</strong> loose pellets. The microbial system can also be<br />

immobilized in the form <strong>of</strong> a film on the wall or as a dense pellet. In the second case<br />

the conversion efficiency is also influenced by transport phenomena. The data given<br />

in Eq. 18 hold only for freely dispersed organisms. When immobilized microorganisms<br />

dominate in a biogas reactor the constants (both saturation and inhibition constants)<br />

are larger.<br />

Eq. 18 can also be used to calculate the combined influence <strong>of</strong> two parameters as<br />

demonstrated in Figure 6.17. This graph shows the gas production as a function <strong>of</strong><br />

Fig. 6.16 Configuration <strong>of</strong> the active microbial system.<br />

Fig. 6.17 Methane production as a function <strong>of</strong> the concentration <strong>of</strong> total acetic acid at different<br />

concentrations <strong>of</strong> total hydrogen sulfide (c HPro = 0).

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