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of VFA are neglected. In a COD-based mass balance, this means that degraded
COD material is converted into methane COD.
3. From the data obtained in the biodegradability survey, estimate the inert fraction
of the organic substrate ( f I ) and the first-order rate coefficient for hydrolysis of the
biodegradable fraction of the organic substrate ( k h ). Discuss the results obtained.
By identifying the biodegradable fraction of the substrate and the hydrolysis
rate coefficient, we can design a continuous stirred tank bioreactor. The extent
of degradation of the substrate we want to achieve is the main variable in
the design of the process, and we therefore aim our design at achieving
60, 70, 80, 90, or 95% degradation of the biodegradable fraction of the substrate
to biogas.
4. Estimate the retention times and reactor volumes required to obtain the required
degrees of degradation.
5. Estimate the potential biogas production (m 3 .h −1 ) and the biogas composition
(vol.% CH 4 and vol.% CO 2 ).
6. Estimate the electricity production (MW) that can be obtained from the biogas
in a CHP plant.
7. Discuss the results obtained in terms of the volume required versus the electric-
ity production.
8. Discuss the additional technology and measures that are needed for successful
implementation of the process. Think about pretreatment methods or technol-
ogies for nutrient recovery, heat integration, etc.
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