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 |
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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. 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.</description><identifier>ISSN: 0043-1354</identifier><identifier>EISSN: 1879-2448</identifier><identifier>DOI: 10.1016/S0043-1354(98)00255-3</identifier><identifier>CODEN: WATRAG</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>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</subject><ispartof>Water research (Oxford), 1999-02, Vol.33 (3), p.681-692</ispartof><rights>1998 Elsevier Science Ltd</rights><rights>1999 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c488t-a78c0adea3986bb21037878cd7d10c5a1929ec42061c4bca0a0f9fe82777c7ea3</citedby><cites>FETCH-LOGICAL-c488t-a78c0adea3986bb21037878cd7d10c5a1929ec42061c4bca0a0f9fe82777c7ea3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0043135498002553$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=1656262$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>Armenante, Piero M.</creatorcontrib><creatorcontrib>Kafkewitz, David</creatorcontrib><creatorcontrib>Lewandowski, Gordon A.</creatorcontrib><creatorcontrib>Jou, Chih-Ju</creatorcontrib><title>Anaerobic–aerobic treatment of halogenated phenolic compounds</title><title>Water research (Oxford)</title><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.</description><subject>2,4,6-trichlorophenol</subject><subject>aerobic treatment</subject><subject>anaerobic treatment</subject><subject>anaerobic–aerobic treatment</subject><subject>Applied sciences</subject><subject>Biological and medical sciences</subject><subject>Biological treatment of waters</subject><subject>bioreactor</subject><subject>Biotechnology</subject><subject>chlorophenol</subject><subject>dichlorophenol</subject><subject>Environment and pollution</subject><subject>Exact sciences and technology</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Industrial applications and implications. Economical aspects</subject><subject>Industrial wastewaters</subject><subject>kinetic modelling</subject><subject>kinetics</subject><subject>mathematical models</subject><subject>Michaelis–Menten parameters</subject><subject>phenols</subject><subject>pollutants</subject><subject>Pollution</subject><subject>reactor</subject><subject>trichlorophenol</subject><subject>Wastewaters</subject><subject>Water treatment and pollution</subject><issn>0043-1354</issn><issn>1879-2448</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1999</creationdate><recordtype>article</recordtype><recordid>eNqF0MtKLDEQBuAgCo6jjyDOQkQXrZVLd5KViHgDwYW6DjXpam3p6YxJzwF35x18Q5_E6Ay6dJUifH9S_IztcjjmwKuTewAlCy5LdWjNEYAoy0KusRE32hZCKbPORj9kk22l9AJZCWlH7PSsR4ph2vqP_--raTJEwmFG_TAJzeQZu_BEPQ5UT-bP1IcuCx9m87Do67TNNhrsEu2szjF7vLx4OL8ubu-ubs7PbguvjBkK1MYD1oTSmmo6FRykNvmu1jUHXyK3wpJXAiru1dQjIDS2ISO01l7n2JgdLN-dx_C6oDS4WZs8dR32FBbJcS1EqYT-G8oKNDdVhuUS-hhSitS4eWxnGN8cB_fVq_vu1X2V5qxx3706mXP7qw8weeyaiL1v02-4KitRicz2lqzB4PApZvJ4L4BLEBasysOYnS4F5d7-tRRd8i31nuo2kh9cHdo_VvkEINGWKg</recordid><startdate>19990201</startdate><enddate>19990201</enddate><creator>Armenante, Piero M.</creator><creator>Kafkewitz, David</creator><creator>Lewandowski, Gordon A.</creator><creator>Jou, Chih-Ju</creator><general>Elsevier Ltd</general><general>Elsevier Science</general><scope>FBQ</scope><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7TV</scope><scope>7UA</scope><scope>C1K</scope></search><sort><creationdate>19990201</creationdate><title>Anaerobic–aerobic treatment of halogenated phenolic compounds</title><author>Armenante, Piero M. ; Kafkewitz, David ; Lewandowski, Gordon A. ; Jou, Chih-Ju</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c488t-a78c0adea3986bb21037878cd7d10c5a1929ec42061c4bca0a0f9fe82777c7ea3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1999</creationdate><topic>2,4,6-trichlorophenol</topic><topic>aerobic treatment</topic><topic>anaerobic treatment</topic><topic>anaerobic–aerobic treatment</topic><topic>Applied sciences</topic><topic>Biological and medical sciences</topic><topic>Biological treatment of waters</topic><topic>bioreactor</topic><topic>Biotechnology</topic><topic>chlorophenol</topic><topic>dichlorophenol</topic><topic>Environment and pollution</topic><topic>Exact sciences and technology</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>Industrial applications and implications. Economical aspects</topic><topic>Industrial wastewaters</topic><topic>kinetic modelling</topic><topic>kinetics</topic><topic>mathematical models</topic><topic>Michaelis–Menten parameters</topic><topic>phenols</topic><topic>pollutants</topic><topic>Pollution</topic><topic>reactor</topic><topic>trichlorophenol</topic><topic>Wastewaters</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Armenante, Piero M.</creatorcontrib><creatorcontrib>Kafkewitz, David</creatorcontrib><creatorcontrib>Lewandowski, Gordon A.</creatorcontrib><creatorcontrib>Jou, Chih-Ju</creatorcontrib><collection>AGRIS</collection><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Aqualine</collection><collection>Pollution Abstracts</collection><collection>Water Resources Abstracts</collection><collection>Environmental Sciences and Pollution Management</collection><jtitle>Water research (Oxford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Armenante, Piero M.</au><au>Kafkewitz, David</au><au>Lewandowski, Gordon A.</au><au>Jou, Chih-Ju</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Anaerobic–aerobic treatment of halogenated phenolic compounds</atitle><jtitle>Water research (Oxford)</jtitle><date>1999-02-01</date><risdate>1999</risdate><volume>33</volume><issue>3</issue><spage>681</spage><epage>692</epage><pages>681-692</pages><issn>0043-1354</issn><eissn>1879-2448</eissn><coden>WATRAG</coden><abstract>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.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/S0043-1354(98)00255-3</doi><tpages>12</tpages></addata></record> |
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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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