Removal of endosulfan in a sequencing batch reactor: addition of granular activated carbon as improvement strategy
A granular activated carbon‐sequencing batch reactor (GAC‐SBR) was used to assess the removal of organochlorine endosulfan pesticide. The reactor operated in three stages: (I) starter and stabilization; (II) addition of 4 mg/L of endosulfan in feed; and (III) a single addition of 1 g/L of GAC to mix...
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description | A granular activated carbon‐sequencing batch reactor (GAC‐SBR) was used to assess the removal of organochlorine endosulfan pesticide. The reactor operated in three stages: (I) starter and stabilization; (II) addition of 4 mg/L of endosulfan in feed; and (III) a single addition of 1 g/L of GAC to mixed liquor. During the 249 days of operation, the removal efficiency of COD was 96 ± 2%; for NH4+‐N 72 ± 1%; and for PO4−3‐P 48 ± 13%. Was eliminated the 79% of endosulfan in stage II and 99% in stage III, not found its metabolite (endosulfan sulphate) in the reactor effluent. A consortium of eight bacterial strains was identified in the reactor stages, assessing five of them in the presence of 4 mg endosulfan/L by growth kinetics. According to the results, the joint action of the consortium and GAC addition is the responsible of eliminating the pesticide. |
doi_str_mv | 10.1111/wej.12637 |
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The reactor operated in three stages: (I) starter and stabilization; (II) addition of 4 mg/L of endosulfan in feed; and (III) a single addition of 1 g/L of GAC to mixed liquor. During the 249 days of operation, the removal efficiency of COD was 96 ± 2%; for NH4+‐N 72 ± 1%; and for PO4−3‐P 48 ± 13%. Was eliminated the 79% of endosulfan in stage II and 99% in stage III, not found its metabolite (endosulfan sulphate) in the reactor effluent. A consortium of eight bacterial strains was identified in the reactor stages, assessing five of them in the presence of 4 mg endosulfan/L by growth kinetics. 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The reactor operated in three stages: (I) starter and stabilization; (II) addition of 4 mg/L of endosulfan in feed; and (III) a single addition of 1 g/L of GAC to mixed liquor. During the 249 days of operation, the removal efficiency of COD was 96 ± 2%; for NH4+‐N 72 ± 1%; and for PO4−3‐P 48 ± 13%. Was eliminated the 79% of endosulfan in stage II and 99% in stage III, not found its metabolite (endosulfan sulphate) in the reactor effluent. A consortium of eight bacterial strains was identified in the reactor stages, assessing five of them in the presence of 4 mg endosulfan/L by growth kinetics. According to the results, the joint action of the consortium and GAC addition is the responsible of eliminating the pesticide.</description><subject>Activated carbon</subject><subject>anoxic‐aerobic treatment</subject><subject>bacteria</subject><subject>Batch reactors</subject><subject>Chlorine compounds</subject><subject>Consortia</subject><subject>Endosulfan</subject><subject>granular activated carbon</subject><subject>growth kinetic</subject><subject>Growth kinetics</subject><subject>Kinetics</subject><subject>Metabolites</subject><subject>Microbiological strains</subject><subject>Organic compounds</subject><subject>organochlorine pesticides</subject><subject>PCB</subject><subject>Pesticides</subject><subject>Phosphates</subject><subject>Polychlorinated biphenyls</subject><subject>Reactors</subject><subject>Removal</subject><subject>Sequencing</subject><subject>Sequencing batch reactor</subject><issn>1747-6585</issn><issn>1747-6593</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><recordid>eNp1UE1LAzEQDaJgrR78BwFPHtomm-wm602KnxQEKXgMs_moW7bZmuy29N-buuLNuczAe2_mzUPompIpTTXb2_WUZgUTJ2hEBReTIi_Z6d8s83N0EeOaEC7Kohih8G437Q4a3DpsvWlj3zjwuPYYcLRfvfW69itcQac_cbCguzbcYTCm7urWH1WrAL5vIOCE1TvorMEaQpVAiLjebEO7sxvrOxy7kNDV4RKdOWiivfrtY7R8fFjOnyeLt6eX-f1iohlLZkvBOVSUGEtJzmWZGSIr7cqM55xZ5jLQLBOEVjKnXEApy4Iabo0rHGgh2RjdDGuTg_RH7NS67YNPF1XGpZCZPC4ao9uBpUMbY7BObUO9gXBQlKhjoiolqn4STdzZwN3XjT38T1QfD6-D4hsRl3j2</recordid><startdate>202102</startdate><enddate>202102</enddate><creator>Reynoso Varela, Andrea</creator><creator>Vázquez Contreras, Fabián P.</creator><creator>de los Santos Villalobos, Sergio</creator><creator>Alvarez Valencia, Luis H.</creator><creator>Ulloa Mercado, Ruth G.</creator><creator>Serrano Palacios, Denisse</creator><general>Wiley Subscription Services, Inc</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QH</scope><scope>7ST</scope><scope>7UA</scope><scope>C1K</scope><scope>F1W</scope><scope>H97</scope><scope>L.G</scope><scope>SOI</scope><orcidid>https://orcid.org/0000-0002-7797-1038</orcidid></search><sort><creationdate>202102</creationdate><title>Removal of endosulfan in a sequencing batch reactor: addition of granular activated carbon as improvement strategy</title><author>Reynoso Varela, Andrea ; 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subjects | Activated carbon anoxic‐aerobic treatment bacteria Batch reactors Chlorine compounds Consortia Endosulfan granular activated carbon growth kinetic Growth kinetics Kinetics Metabolites Microbiological strains Organic compounds organochlorine pesticides PCB Pesticides Phosphates Polychlorinated biphenyls Reactors Removal Sequencing Sequencing batch reactor |
title | Removal of endosulfan in a sequencing batch reactor: addition of granular activated carbon as improvement strategy |
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