A comprehensive dynamic model is presented that simulates methanogenes
is and sulfate reduction in a continuously stirred tank reactor (CSTR)
. This model incorporates the complex chemistry of anaerobic systems.
A salient feature of the model is its ability to predict the effluent
concentrations of the various chemical species in the reactor directly
from the feed conditions. Precipitation equilibria of the essential m
etals were also incorporated in the model. Model predictions were comp
ared with results from steady-state and batch spike experiments. A det
ailed sensitivity analysis of the effect of key model parameters on mo
del performance was conducted. The model was able to predict both the
steady-state and the transient batch spike experimental data fairly we
ll.