Kinetics of phenol degradation by activated sludge: Value of measurements in a batch reactor

Abstract

Kinetic measurements on the degradation of phenol in a batch reactor were done at 20°C using an activated sludge taken from a continuous reactor where the process had shown Monod-type kinetics without substrate inhibition. When employing a sludge sample, adapted to the substrate steady concentration C s 1, for runs with initial substrate concentration C s 0, observed batch rates were as high as expected for C s 0 = C s 1, but lower than expected in runs carried out at C s 0 > C s1 1, with indications of a transient inhibitory effect instead of a positive response to the increased substrate concentration. It is concluded that kinetic data collected in a batch reactor are of limited value for the design of a continuous biodegradation process.