Using sequentially coupled UV/H2O2-biologic systems to treat industrial wastewater with high carbon and nitrogen contents
[Display omitted] •The design and operation parameters of a UV/H2O2-biological system were established.•Nitrogen transformations were investigated throughout the UV/H2O2-biological process.•Hybrid process removed over than 60 % of persistent dissolved organic matter.•Biological denitrification stage...
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creator | Ortiz-Marin, A.D. Amabilis-Sosa, L.E. Bandala, E.R. Guillén-Garcés, R.A. Treviño-Quintanilla, L.G. Roé-Sosa, A. Moeller-Chávez, G.E. |
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•The design and operation parameters of a UV/H2O2-biological system were established.•Nitrogen transformations were investigated throughout the UV/H2O2-biological process.•Hybrid process removed over than 60 % of persistent dissolved organic matter.•Biological denitrification stage has achieved more than 80 % of efficiency.
This study evaluated the performance of a sequentially coupled UV/H2O2-anoxic system to treat industrial wastewater (IWW). Initial IWW characterization showed a high chemical oxygen demand (COD) load (13,261 mg L−1, 6,880 mg L−1 of total organic carbon (TOC), 569 mg L−1 of total nitrogen (TN), and an alkaline pH (9.1 ± 1.51). Using advanced oxidation processes (AOPs), removal efficiencies of 49.4 % of COD and 85 % of total organic carbon (TOC) were achieved after 60 min of UV-C irradiation (82 W m−2) using a H2O2/COD ratio of 0.78:1. Under these conditions, a 50 % transformation of TN into nitrites and nitrates (NO2+NO3)-N was also observed. After the AOP, the partially treated IWW was mixed with municipal wastewater (MWW) at ratio of 1:10, based on toxicity test results, and then used as the influent of the biological process. The biological process consisted of anoxic suspended and attached biomass coupled sequentially after the UV/H2O2 system. Both biological systems (attached and suspended biomass reactors) efficiently removed (NO2+NO3)-N, achieving 85 % removal of TN, 41.8 % removal of TOC, and 49.2 % removal of COD and denitrification process was found to occur after the AOP through the biological systems. In addition, pH values ranging from 6 to 7.6 were observed after the biological treatment, which suggests that the resulting effluent could be treated using conventional water treatment. |
doi_str_mv | 10.1016/j.psep.2020.02.020 |
format | Article |
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•The design and operation parameters of a UV/H2O2-biological system were established.•Nitrogen transformations were investigated throughout the UV/H2O2-biological process.•Hybrid process removed over than 60 % of persistent dissolved organic matter.•Biological denitrification stage has achieved more than 80 % of efficiency.
This study evaluated the performance of a sequentially coupled UV/H2O2-anoxic system to treat industrial wastewater (IWW). Initial IWW characterization showed a high chemical oxygen demand (COD) load (13,261 mg L−1, 6,880 mg L−1 of total organic carbon (TOC), 569 mg L−1 of total nitrogen (TN), and an alkaline pH (9.1 ± 1.51). Using advanced oxidation processes (AOPs), removal efficiencies of 49.4 % of COD and 85 % of total organic carbon (TOC) were achieved after 60 min of UV-C irradiation (82 W m−2) using a H2O2/COD ratio of 0.78:1. Under these conditions, a 50 % transformation of TN into nitrites and nitrates (NO2+NO3)-N was also observed. After the AOP, the partially treated IWW was mixed with municipal wastewater (MWW) at ratio of 1:10, based on toxicity test results, and then used as the influent of the biological process. The biological process consisted of anoxic suspended and attached biomass coupled sequentially after the UV/H2O2 system. Both biological systems (attached and suspended biomass reactors) efficiently removed (NO2+NO3)-N, achieving 85 % removal of TN, 41.8 % removal of TOC, and 49.2 % removal of COD and denitrification process was found to occur after the AOP through the biological systems. In addition, pH values ranging from 6 to 7.6 were observed after the biological treatment, which suggests that the resulting effluent could be treated using conventional water treatment.</description><identifier>ISSN: 0957-5820</identifier><identifier>EISSN: 1744-3598</identifier><identifier>DOI: 10.1016/j.psep.2020.02.020</identifier><language>eng</language><publisher>Rugby: Elsevier B.V</publisher><subject>Anoxic systems ; Biological activity ; Biological treatment ; Biomass ; Carbon ; Chemical oxygen demand ; Denitrification ; Effluent treatment ; Hydrogen peroxide ; Industrial wastes ; Industrial wastewater ; Irradiation ; Municipal wastewater ; Nitrates ; Nitrites ; Nitrogen dioxide ; Nitrogen transformations ; Organic carbon ; Oxidation ; pH effects ; Total organic carbon ; Toxicity ; Toxicity testing ; Ultraviolet radiation ; UV/H2O2 ; Wastewater ; Wastewater treatment ; Water treatment</subject><ispartof>Process safety and environmental protection, 2020-05, Vol.137, p.192-199</ispartof><rights>2020 Institution of Chemical Engineers</rights><rights>Copyright Elsevier Science Ltd. May 2020</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c328t-6f5169394aff809eb0931924aac8757e6328dac2379e21ba92246795065c870e3</citedby><cites>FETCH-LOGICAL-c328t-6f5169394aff809eb0931924aac8757e6328dac2379e21ba92246795065c870e3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1016/j.psep.2020.02.020$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,3548,27923,27924,45994</link.rule.ids></links><search><creatorcontrib>Ortiz-Marin, A.D.</creatorcontrib><creatorcontrib>Amabilis-Sosa, L.E.</creatorcontrib><creatorcontrib>Bandala, E.R.</creatorcontrib><creatorcontrib>Guillén-Garcés, R.A.</creatorcontrib><creatorcontrib>Treviño-Quintanilla, L.G.</creatorcontrib><creatorcontrib>Roé-Sosa, A.</creatorcontrib><creatorcontrib>Moeller-Chávez, G.E.</creatorcontrib><title>Using sequentially coupled UV/H2O2-biologic systems to treat industrial wastewater with high carbon and nitrogen contents</title><title>Process safety and environmental protection</title><description>[Display omitted]
•The design and operation parameters of a UV/H2O2-biological system were established.•Nitrogen transformations were investigated throughout the UV/H2O2-biological process.•Hybrid process removed over than 60 % of persistent dissolved organic matter.•Biological denitrification stage has achieved more than 80 % of efficiency.
This study evaluated the performance of a sequentially coupled UV/H2O2-anoxic system to treat industrial wastewater (IWW). Initial IWW characterization showed a high chemical oxygen demand (COD) load (13,261 mg L−1, 6,880 mg L−1 of total organic carbon (TOC), 569 mg L−1 of total nitrogen (TN), and an alkaline pH (9.1 ± 1.51). Using advanced oxidation processes (AOPs), removal efficiencies of 49.4 % of COD and 85 % of total organic carbon (TOC) were achieved after 60 min of UV-C irradiation (82 W m−2) using a H2O2/COD ratio of 0.78:1. Under these conditions, a 50 % transformation of TN into nitrites and nitrates (NO2+NO3)-N was also observed. After the AOP, the partially treated IWW was mixed with municipal wastewater (MWW) at ratio of 1:10, based on toxicity test results, and then used as the influent of the biological process. The biological process consisted of anoxic suspended and attached biomass coupled sequentially after the UV/H2O2 system. Both biological systems (attached and suspended biomass reactors) efficiently removed (NO2+NO3)-N, achieving 85 % removal of TN, 41.8 % removal of TOC, and 49.2 % removal of COD and denitrification process was found to occur after the AOP through the biological systems. In addition, pH values ranging from 6 to 7.6 were observed after the biological treatment, which suggests that the resulting effluent could be treated using conventional water treatment.</description><subject>Anoxic systems</subject><subject>Biological activity</subject><subject>Biological treatment</subject><subject>Biomass</subject><subject>Carbon</subject><subject>Chemical oxygen demand</subject><subject>Denitrification</subject><subject>Effluent treatment</subject><subject>Hydrogen peroxide</subject><subject>Industrial wastes</subject><subject>Industrial wastewater</subject><subject>Irradiation</subject><subject>Municipal wastewater</subject><subject>Nitrates</subject><subject>Nitrites</subject><subject>Nitrogen dioxide</subject><subject>Nitrogen transformations</subject><subject>Organic carbon</subject><subject>Oxidation</subject><subject>pH effects</subject><subject>Total organic carbon</subject><subject>Toxicity</subject><subject>Toxicity testing</subject><subject>Ultraviolet radiation</subject><subject>UV/H2O2</subject><subject>Wastewater</subject><subject>Wastewater treatment</subject><subject>Water treatment</subject><issn>0957-5820</issn><issn>1744-3598</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2020</creationdate><recordtype>article</recordtype><recordid>eNp9UE1rGzEQFSGFOmn_QE-CnNcZza52V5BLCW1cCORS9ypk7awts5E2klzjfx8Z5xx4MId5HzOPsR8ClgJEe79fzonmJQLCErAArthCdE1T1VL112wBSnaV7BG-spuU9gAgsBMLdlon57c80duBfHZmmk7chsM80cDX_-5X-ILVxoUpbJ3l6ZQyvSaeA8-RTObOD4eUY5Hxoym7o8kU-dHlHd-57Y5bEzfBc-MH7l2OYUu-uPtcotI39mU0U6LvH_OWrX__-vu4qp5fnv48_nyubI19rtpRilbVqjHj2IOiDahaKGyMsX0nO2oLazAW604Rio1RiE3bKQmtLASg-pbdXXznGMqTKet9OERfIjU2NUqpALvCwgvLxpBSpFHP0b2aeNIC9LlivdfnivW5Yg1YAEX0cBFRuf-_o6iTdeQtDS6SzXoI7jP5Ozb_heg</recordid><startdate>202005</startdate><enddate>202005</enddate><creator>Ortiz-Marin, A.D.</creator><creator>Amabilis-Sosa, L.E.</creator><creator>Bandala, E.R.</creator><creator>Guillén-Garcés, R.A.</creator><creator>Treviño-Quintanilla, L.G.</creator><creator>Roé-Sosa, A.</creator><creator>Moeller-Chávez, G.E.</creator><general>Elsevier B.V</general><general>Elsevier Science Ltd</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7ST</scope><scope>7TB</scope><scope>7U7</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>KR7</scope><scope>SOI</scope></search><sort><creationdate>202005</creationdate><title>Using sequentially coupled UV/H2O2-biologic systems to treat industrial wastewater with high carbon and nitrogen contents</title><author>Ortiz-Marin, A.D. ; Amabilis-Sosa, L.E. ; Bandala, E.R. ; Guillén-Garcés, R.A. ; Treviño-Quintanilla, L.G. ; Roé-Sosa, A. ; Moeller-Chávez, G.E.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c328t-6f5169394aff809eb0931924aac8757e6328dac2379e21ba92246795065c870e3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2020</creationdate><topic>Anoxic systems</topic><topic>Biological activity</topic><topic>Biological treatment</topic><topic>Biomass</topic><topic>Carbon</topic><topic>Chemical oxygen demand</topic><topic>Denitrification</topic><topic>Effluent treatment</topic><topic>Hydrogen peroxide</topic><topic>Industrial wastes</topic><topic>Industrial wastewater</topic><topic>Irradiation</topic><topic>Municipal wastewater</topic><topic>Nitrates</topic><topic>Nitrites</topic><topic>Nitrogen dioxide</topic><topic>Nitrogen transformations</topic><topic>Organic carbon</topic><topic>Oxidation</topic><topic>pH effects</topic><topic>Total organic carbon</topic><topic>Toxicity</topic><topic>Toxicity testing</topic><topic>Ultraviolet radiation</topic><topic>UV/H2O2</topic><topic>Wastewater</topic><topic>Wastewater treatment</topic><topic>Water treatment</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Ortiz-Marin, A.D.</creatorcontrib><creatorcontrib>Amabilis-Sosa, L.E.</creatorcontrib><creatorcontrib>Bandala, E.R.</creatorcontrib><creatorcontrib>Guillén-Garcés, R.A.</creatorcontrib><creatorcontrib>Treviño-Quintanilla, L.G.</creatorcontrib><creatorcontrib>Roé-Sosa, A.</creatorcontrib><creatorcontrib>Moeller-Chávez, G.E.</creatorcontrib><collection>CrossRef</collection><collection>Environment Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Toxicology Abstracts</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>Engineering Research Database</collection><collection>Civil Engineering Abstracts</collection><collection>Environment Abstracts</collection><jtitle>Process safety and environmental protection</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Ortiz-Marin, A.D.</au><au>Amabilis-Sosa, L.E.</au><au>Bandala, E.R.</au><au>Guillén-Garcés, R.A.</au><au>Treviño-Quintanilla, L.G.</au><au>Roé-Sosa, A.</au><au>Moeller-Chávez, G.E.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Using sequentially coupled UV/H2O2-biologic systems to treat industrial wastewater with high carbon and nitrogen contents</atitle><jtitle>Process safety and environmental protection</jtitle><date>2020-05</date><risdate>2020</risdate><volume>137</volume><spage>192</spage><epage>199</epage><pages>192-199</pages><issn>0957-5820</issn><eissn>1744-3598</eissn><abstract>[Display omitted]
•The design and operation parameters of a UV/H2O2-biological system were established.•Nitrogen transformations were investigated throughout the UV/H2O2-biological process.•Hybrid process removed over than 60 % of persistent dissolved organic matter.•Biological denitrification stage has achieved more than 80 % of efficiency.
This study evaluated the performance of a sequentially coupled UV/H2O2-anoxic system to treat industrial wastewater (IWW). Initial IWW characterization showed a high chemical oxygen demand (COD) load (13,261 mg L−1, 6,880 mg L−1 of total organic carbon (TOC), 569 mg L−1 of total nitrogen (TN), and an alkaline pH (9.1 ± 1.51). Using advanced oxidation processes (AOPs), removal efficiencies of 49.4 % of COD and 85 % of total organic carbon (TOC) were achieved after 60 min of UV-C irradiation (82 W m−2) using a H2O2/COD ratio of 0.78:1. Under these conditions, a 50 % transformation of TN into nitrites and nitrates (NO2+NO3)-N was also observed. After the AOP, the partially treated IWW was mixed with municipal wastewater (MWW) at ratio of 1:10, based on toxicity test results, and then used as the influent of the biological process. The biological process consisted of anoxic suspended and attached biomass coupled sequentially after the UV/H2O2 system. Both biological systems (attached and suspended biomass reactors) efficiently removed (NO2+NO3)-N, achieving 85 % removal of TN, 41.8 % removal of TOC, and 49.2 % removal of COD and denitrification process was found to occur after the AOP through the biological systems. In addition, pH values ranging from 6 to 7.6 were observed after the biological treatment, which suggests that the resulting effluent could be treated using conventional water treatment.</abstract><cop>Rugby</cop><pub>Elsevier B.V</pub><doi>10.1016/j.psep.2020.02.020</doi><tpages>8</tpages></addata></record> |
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subjects | Anoxic systems Biological activity Biological treatment Biomass Carbon Chemical oxygen demand Denitrification Effluent treatment Hydrogen peroxide Industrial wastes Industrial wastewater Irradiation Municipal wastewater Nitrates Nitrites Nitrogen dioxide Nitrogen transformations Organic carbon Oxidation pH effects Total organic carbon Toxicity Toxicity testing Ultraviolet radiation UV/H2O2 Wastewater Wastewater treatment Water treatment |
title | Using sequentially coupled UV/H2O2-biologic systems to treat industrial wastewater with high carbon and nitrogen contents |
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