Selection of growth rate model for activated sludges treating phenol

Research was undertaken for the purpose of selecting a growth rate model, i.e. a function relating specific growth rate, μ, to substrate concentration, S, for acclimated heterogeneous microbial populations metabolizing a phenolic waste and to gain an insight into the expected average and range of values of the kinetic “constants” for the selected model. Various sources of seed populations were employed and batch growth curves were generated using phenol as sole source of carbon. Comparison of the fit of the data obtained from 113 growth curves to five inhibition functions failed to distinguish a function which was statistically superior to the others. Since the Haldane equation proved to be the most readily adapted to curve-fitting procedures and insertion into mass balance equations for reactor performance, it was selected as the best representation of the experimental data. The values of the three pertinent biokinetic constants were as follows: μ_max, range = 0.08–0.36 h^?1, mean = 0.19 h^?1; K_S, range = 1.3–266 mg l^?1, mean = 75 mg l^?1; K_i, range = 66–1463 mg l^?1, mean 449 mg l^?1. Analysis of chemostat performance using growth constants determined in separate batch growth studies with seed from the chemostat showed that reasonably accurate prediction of the dilution rate at which the system attains μ1, the peak or critical specific growth rate designated by the Haldane equation, could be made. This finding indicates that batch growth rate data can be used for predictive control of activated sludge reactors treating toxic wastes.