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 Cs1, for runs with initial substrate concentration Cs0, observed batch rates were as high as expected for Cs0 = Cs1, but lower than expected in runs carried out at Cs0 > Cs11, 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.

Kinetics of Phenol Degradation by Activated Sludge: Value of Measurements in a Batch Reactor / P. Beltrame, P.L. Beltrame, P. Carniti, D. Pitea. - In: WATER RESEARCH. - ISSN 0043-1354. - 13:12(1979), pp. 1305-1309.

Kinetics of Phenol Degradation by Activated Sludge: Value of Measurements in a Batch Reactor

P. Beltrame
Primo
;
P. Carniti
Penultimo
;
1979

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 Cs1, for runs with initial substrate concentration Cs0, observed batch rates were as high as expected for Cs0 = Cs1, but lower than expected in runs carried out at Cs0 > Cs11, 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.
Settore CHIM/02 - Chimica Fisica
1979
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/2434/197159
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