Anaerobic–aerobic treatment of halogenated phenolic compounds

2,4,6-trichlorophenol (2,4,6-TCP) was successfully and completely degraded in a two-stage anaerobic–aerobic biological process in which the initial step was conducted anaerobically, resulting in the reductive dechlorination of the target compound to 2,4-dichlorophenol (2,4-DCP), and then 4-chlorophe...

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Veröffentlicht in:Water research (Oxford) 1999-02, Vol.33 (3), p.681-692
Hauptverfasser: Armenante, Piero M., Kafkewitz, David, Lewandowski, Gordon A., Jou, Chih-Ju
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creator Armenante, Piero M.
Kafkewitz, David
Lewandowski, Gordon A.
Jou, Chih-Ju
description 2,4,6-trichlorophenol (2,4,6-TCP) was successfully and completely degraded in a two-stage anaerobic–aerobic biological process in which the initial step was conducted anaerobically, resulting in the reductive dechlorination of the target compound to 2,4-dichlorophenol (2,4-DCP), and then 4-chlorophenol (4-CP). Stoichiometric conversion of 2,4,6-TCP to 4-CP was achieved. The latter compound was then attacked and completely degraded aerobically in a second stage. The effects of parameters such as temperature and pH were determined for individual components of the process. The process was studied in serum bottles and shake flasks, and in anaerobic and aerobic bioreactors operating in both batch and continuous modes. A sequential anaerobic–aerobic bioreactor system was assembled, in which complete 2,4,6-TCP degradation was achieved. A mathematical model was developed to describe both anaerobic and aerobic processes, and the complete system. The model assumed that 2,4,6-TCP and 2,4-TCP could be anaerobically attacked according to a sequential irreversible reductive dechlorination reaction scheme based on Michaelis–Menten kinetics. A similar model was used to quantify aerobic degradation. The kinetic parameters for each step were obtained in independent batch experiments with suspended cultures, and were internally consistent. The model was able to predict the experimental results, which lends validity to the postulated kinetics mechanism.
doi_str_mv 10.1016/S0043-1354(98)00255-3
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Stoichiometric conversion of 2,4,6-TCP to 4-CP was achieved. The latter compound was then attacked and completely degraded aerobically in a second stage. The effects of parameters such as temperature and pH were determined for individual components of the process. The process was studied in serum bottles and shake flasks, and in anaerobic and aerobic bioreactors operating in both batch and continuous modes. A sequential anaerobic–aerobic bioreactor system was assembled, in which complete 2,4,6-TCP degradation was achieved. A mathematical model was developed to describe both anaerobic and aerobic processes, and the complete system. The model assumed that 2,4,6-TCP and 2,4-TCP could be anaerobically attacked according to a sequential irreversible reductive dechlorination reaction scheme based on Michaelis–Menten kinetics. A similar model was used to quantify aerobic degradation. 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subjects 2,4,6-trichlorophenol
aerobic treatment
anaerobic treatment
anaerobic–aerobic treatment
Applied sciences
Biological and medical sciences
Biological treatment of waters
bioreactor
Biotechnology
chlorophenol
dichlorophenol
Environment and pollution
Exact sciences and technology
Fundamental and applied biological sciences. Psychology
Industrial applications and implications. Economical aspects
Industrial wastewaters
kinetic modelling
kinetics
mathematical models
Michaelis–Menten parameters
phenols
pollutants
Pollution
reactor
trichlorophenol
Wastewaters
Water treatment and pollution
title Anaerobic–aerobic treatment of halogenated phenolic compounds
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