Modeling of Biogas Reactors
Modeling of Biogas Reactors
Modeling of Biogas Reactors
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170 6 <strong>Modeling</strong> <strong>of</strong> <strong>Biogas</strong> <strong>Reactors</strong><br />
Fig. 6.6 Calibration <strong>of</strong> the silicon membrane probe coupled to mass spectrometer measuring<br />
the dissolved CO 2 in desalinated water (after Polomski, 1998).<br />
means <strong>of</strong> isocratic cation exchange chromatography. For the detection <strong>of</strong> betaine<br />
and N,N-DMG an ultraviolet detector was used. All other substances were detected<br />
by conductivity.<br />
Besides other organic components, such as acetic and propionic acid, betaine is<br />
the dominant organic substance in the wastewater. Up to 33% <strong>of</strong> the TOC is represented<br />
by betaine. The use <strong>of</strong> HPLC analysis combined with an automated ultrafiltration<br />
setup for online process monitoring gives interesting information about the<br />
dynamic behavior <strong>of</strong> the anaerobic process, as demonstrated in Figure 6.7. The<br />
graphs show the effect <strong>of</strong> hydrogen sulfide elimination from the fermentation broth.<br />
The concentration <strong>of</strong> undissociated H 2S was decreased by a factor <strong>of</strong> 2 (from 300 to<br />
150 mg L –1 ). During the same time biogas production increased. The concentration<br />
<strong>of</strong> acetic acid decreased while the other acids measured remained more or less<br />
stable. Betaine was completely degraded only at lower H 2S concentrations. Interestingly,<br />
the concentration <strong>of</strong> N,N-DMG, which is a metabolic product <strong>of</strong> the anaerobic<br />
degradation <strong>of</strong> betaine, is also decreased.<br />
6.3<br />
Kinetics<br />
The anaerobic degradation <strong>of</strong> organic substances is performed in a sequence <strong>of</strong><br />
biological reactions in a synthrophic cooperation <strong>of</strong> different microorganisms