Textiles wastewater treatment using anoxic filter bed and biological wriggle bed-ozone biological aerated filter
In this study, the performance of the anoxic filter bed and biological wriggle bed-ozone biological aerated filter (AFB-BWB-O3-BAF) process treating real textile dyeing wastewater was investigated. After more than 2month process operation, the average effluent COD concentration of the AFB, BWB, O3-B...
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| Veröffentlicht in: | Bioresource technology 2011-02, Vol.102 (4), p.3748-3753 |
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| creator | Fu, Zhimin Zhang, Yugao Wang, Xiaojun |
| description | In this study, the performance of the anoxic filter bed and biological wriggle bed-ozone biological aerated filter (AFB-BWB-O3-BAF) process treating real textile dyeing wastewater was investigated. After more than 2month process operation, the average effluent COD concentration of the AFB, BWB, O3-BAF were 704.8mg/L, 294.6mg/L and 128.8mg/L, with HRT being 8.1–7.7h, 9.2h and 5.45h, respectively. Results showed that the effluent COD concentration of the AFB decreased with new carriers added and the average removal COD efficiency was 20.2%. During operation conditions, HRT of the BWB and O3-BAF was increased, resulting in a decrease in the effluent COD concentration. However, on increasing the HRT, the COD reduction capability expressed by the unit carrier COD removal loading of the BWB reactor increased, while that of the O3-BAF reactor decreased. This study is a beneficial attempt to utilize the AFB-BWB-O3-BAF combine process for textile wastewater treatment. |
| doi_str_mv | 10.1016/j.biortech.2010.12.002 |
| format | Article |
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After more than 2month process operation, the average effluent COD concentration of the AFB, BWB, O3-BAF were 704.8mg/L, 294.6mg/L and 128.8mg/L, with HRT being 8.1–7.7h, 9.2h and 5.45h, respectively. Results showed that the effluent COD concentration of the AFB decreased with new carriers added and the average removal COD efficiency was 20.2%. During operation conditions, HRT of the BWB and O3-BAF was increased, resulting in a decrease in the effluent COD concentration. However, on increasing the HRT, the COD reduction capability expressed by the unit carrier COD removal loading of the BWB reactor increased, while that of the O3-BAF reactor decreased. This study is a beneficial attempt to utilize the AFB-BWB-O3-BAF combine process for textile wastewater treatment.</description><identifier>ISSN: 0960-8524</identifier><identifier>EISSN: 1873-2976</identifier><identifier>DOI: 10.1016/j.biortech.2010.12.002</identifier><identifier>PMID: 21186119</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Aerated ; Applied sciences ; Biodegradation treatment ; Biodegradation, Environmental ; Biological ; Biological and medical sciences ; Bioreactors ; Biotechnology ; Biotechnology - methods ; Carriers ; Coloring Agents - chemistry ; Crack opening displacement ; Effluents ; Equipment Design ; Exact sciences and technology ; Fundamental and applied biological sciences. Psychology ; Hydrogen-Ion Concentration ; Hydrolysis ; Industrial Waste ; Nephelometry and Turbidimetry ; Oxygen - chemistry ; Ozone ; Ozone oxidation ; Pollution ; Reactors ; Sulfate elimination ; Sulfates ; Temperature ; Textile wastewater ; Textiles ; Waste water ; Wastewater treatment ; Wastewaters ; Water Purification - methods ; Water treatment and pollution</subject><ispartof>Bioresource technology, 2011-02, Vol.102 (4), p.3748-3753</ispartof><rights>2010 Elsevier Ltd</rights><rights>2015 INIST-CNRS</rights><rights>Copyright © 2010 Elsevier Ltd. All rights reserved.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c486t-695e9c1c365604f243a260e09fa745d72ba6e4277082bdeb9224ba2873714c993</citedby><cites>FETCH-LOGICAL-c486t-695e9c1c365604f243a260e09fa745d72ba6e4277082bdeb9224ba2873714c993</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0960852410019322$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=23828678$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/21186119$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Fu, Zhimin</creatorcontrib><creatorcontrib>Zhang, Yugao</creatorcontrib><creatorcontrib>Wang, Xiaojun</creatorcontrib><title>Textiles wastewater treatment using anoxic filter bed and biological wriggle bed-ozone biological aerated filter</title><title>Bioresource technology</title><addtitle>Bioresour Technol</addtitle><description>In this study, the performance of the anoxic filter bed and biological wriggle bed-ozone biological aerated filter (AFB-BWB-O3-BAF) process treating real textile dyeing wastewater was investigated. After more than 2month process operation, the average effluent COD concentration of the AFB, BWB, O3-BAF were 704.8mg/L, 294.6mg/L and 128.8mg/L, with HRT being 8.1–7.7h, 9.2h and 5.45h, respectively. Results showed that the effluent COD concentration of the AFB decreased with new carriers added and the average removal COD efficiency was 20.2%. During operation conditions, HRT of the BWB and O3-BAF was increased, resulting in a decrease in the effluent COD concentration. However, on increasing the HRT, the COD reduction capability expressed by the unit carrier COD removal loading of the BWB reactor increased, while that of the O3-BAF reactor decreased. This study is a beneficial attempt to utilize the AFB-BWB-O3-BAF combine process for textile wastewater treatment.</description><subject>Aerated</subject><subject>Applied sciences</subject><subject>Biodegradation treatment</subject><subject>Biodegradation, Environmental</subject><subject>Biological</subject><subject>Biological and medical sciences</subject><subject>Bioreactors</subject><subject>Biotechnology</subject><subject>Biotechnology - methods</subject><subject>Carriers</subject><subject>Coloring Agents - chemistry</subject><subject>Crack opening displacement</subject><subject>Effluents</subject><subject>Equipment Design</subject><subject>Exact sciences and technology</subject><subject>Fundamental and applied biological sciences. Psychology</subject><subject>Hydrogen-Ion Concentration</subject><subject>Hydrolysis</subject><subject>Industrial Waste</subject><subject>Nephelometry and Turbidimetry</subject><subject>Oxygen - chemistry</subject><subject>Ozone</subject><subject>Ozone oxidation</subject><subject>Pollution</subject><subject>Reactors</subject><subject>Sulfate elimination</subject><subject>Sulfates</subject><subject>Temperature</subject><subject>Textile wastewater</subject><subject>Textiles</subject><subject>Waste water</subject><subject>Wastewater treatment</subject><subject>Wastewaters</subject><subject>Water Purification - methods</subject><subject>Water treatment and pollution</subject><issn>0960-8524</issn><issn>1873-2976</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2011</creationdate><recordtype>article</recordtype><sourceid>EIF</sourceid><recordid>eNqFkU1v1DAQhi0EokvhL5RcEFyyeBzHHzdQxZdUiQPt2XKcSfAqGy-2t1v49TjaLXCiJ0szz_vOeF5CLoCugYJ4u1l3PsSM7vua0aXI1pSyR2QFSjY101I8JiuqBa1Vy_gZeZbShlLagGRPyRkDUAJAr8juGu-ynzBVB5syHmzGWOWINm9xztU--Xms7BzuvKsGPy3dDvtS6auywBRG7-xUHaIfxwmXVh1-hRn_bVqMxbU_yZ-TJ4OdEr44vefk5uOH68vP9dXXT18u31_VjiuRa6Fb1A5cI1pB-cB4Y5mgSPVgJW97yTorkDMpqWJdj51mjHeWlc9L4E7r5py8PvruYvixx5TN1ieH02RnDPtkVAtclgPJh0kuNAWpaSHf_JcEKSW0ILkoqDiiLoaUIg5mF_3Wxp8GqFkSNBtzn6BZEjTATEmwCC9OM_bdFvs_svvICvDqBNhUzjtEOzuf_nKNYkpIVbiXR26wwdgxFubmW5nU0GLS8hYK8e5IYMnh1mM0yXmcHfY-osumD_6hbX8DmWLGSQ</recordid><startdate>20110201</startdate><enddate>20110201</enddate><creator>Fu, Zhimin</creator><creator>Zhang, Yugao</creator><creator>Wang, Xiaojun</creator><general>Elsevier Ltd</general><general>[New York, NY]: Elsevier Ltd</general><general>Elsevier</general><scope>FBQ</scope><scope>IQODW</scope><scope>CGR</scope><scope>CUY</scope><scope>CVF</scope><scope>ECM</scope><scope>EIF</scope><scope>NPM</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7SU</scope><scope>7TB</scope><scope>8FD</scope><scope>C1K</scope><scope>FR3</scope><scope>KR7</scope><scope>7X8</scope><scope>7QH</scope><scope>7QO</scope><scope>7ST</scope><scope>7UA</scope><scope>P64</scope><scope>SOI</scope></search><sort><creationdate>20110201</creationdate><title>Textiles wastewater treatment using anoxic filter bed and biological wriggle bed-ozone biological aerated filter</title><author>Fu, Zhimin ; Zhang, Yugao ; Wang, Xiaojun</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c486t-695e9c1c365604f243a260e09fa745d72ba6e4277082bdeb9224ba2873714c993</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2011</creationdate><topic>Aerated</topic><topic>Applied sciences</topic><topic>Biodegradation treatment</topic><topic>Biodegradation, Environmental</topic><topic>Biological</topic><topic>Biological and medical sciences</topic><topic>Bioreactors</topic><topic>Biotechnology</topic><topic>Biotechnology - methods</topic><topic>Carriers</topic><topic>Coloring Agents - chemistry</topic><topic>Crack opening displacement</topic><topic>Effluents</topic><topic>Equipment Design</topic><topic>Exact sciences and technology</topic><topic>Fundamental and applied biological sciences. Psychology</topic><topic>Hydrogen-Ion Concentration</topic><topic>Hydrolysis</topic><topic>Industrial Waste</topic><topic>Nephelometry and Turbidimetry</topic><topic>Oxygen - chemistry</topic><topic>Ozone</topic><topic>Ozone oxidation</topic><topic>Pollution</topic><topic>Reactors</topic><topic>Sulfate elimination</topic><topic>Sulfates</topic><topic>Temperature</topic><topic>Textile wastewater</topic><topic>Textiles</topic><topic>Waste water</topic><topic>Wastewater treatment</topic><topic>Wastewaters</topic><topic>Water Purification - methods</topic><topic>Water treatment and pollution</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Fu, Zhimin</creatorcontrib><creatorcontrib>Zhang, Yugao</creatorcontrib><creatorcontrib>Wang, Xiaojun</creatorcontrib><collection>AGRIS</collection><collection>Pascal-Francis</collection><collection>Medline</collection><collection>MEDLINE</collection><collection>MEDLINE (Ovid)</collection><collection>MEDLINE</collection><collection>MEDLINE</collection><collection>PubMed</collection><collection>CrossRef</collection><collection>Environmental Engineering Abstracts</collection><collection>Mechanical & Transportation Engineering 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>MEDLINE - Academic</collection><collection>Aqualine</collection><collection>Biotechnology Research Abstracts</collection><collection>Environment Abstracts</collection><collection>Water Resources Abstracts</collection><collection>Biotechnology and BioEngineering Abstracts</collection><collection>Environment Abstracts</collection><jtitle>Bioresource technology</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Fu, Zhimin</au><au>Zhang, Yugao</au><au>Wang, Xiaojun</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Textiles wastewater treatment using anoxic filter bed and biological wriggle bed-ozone biological aerated filter</atitle><jtitle>Bioresource technology</jtitle><addtitle>Bioresour Technol</addtitle><date>2011-02-01</date><risdate>2011</risdate><volume>102</volume><issue>4</issue><spage>3748</spage><epage>3753</epage><pages>3748-3753</pages><issn>0960-8524</issn><eissn>1873-2976</eissn><abstract>In this study, the performance of the anoxic filter bed and biological wriggle bed-ozone biological aerated filter (AFB-BWB-O3-BAF) process treating real textile dyeing wastewater was investigated. After more than 2month process operation, the average effluent COD concentration of the AFB, BWB, O3-BAF were 704.8mg/L, 294.6mg/L and 128.8mg/L, with HRT being 8.1–7.7h, 9.2h and 5.45h, respectively. Results showed that the effluent COD concentration of the AFB decreased with new carriers added and the average removal COD efficiency was 20.2%. During operation conditions, HRT of the BWB and O3-BAF was increased, resulting in a decrease in the effluent COD concentration. However, on increasing the HRT, the COD reduction capability expressed by the unit carrier COD removal loading of the BWB reactor increased, while that of the O3-BAF reactor decreased. This study is a beneficial attempt to utilize the AFB-BWB-O3-BAF combine process for textile wastewater treatment.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><pmid>21186119</pmid><doi>10.1016/j.biortech.2010.12.002</doi><tpages>6</tpages></addata></record> |
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| subjects | Aerated Applied sciences Biodegradation treatment Biodegradation, Environmental Biological Biological and medical sciences Bioreactors Biotechnology Biotechnology - methods Carriers Coloring Agents - chemistry Crack opening displacement Effluents Equipment Design Exact sciences and technology Fundamental and applied biological sciences. Psychology Hydrogen-Ion Concentration Hydrolysis Industrial Waste Nephelometry and Turbidimetry Oxygen - chemistry Ozone Ozone oxidation Pollution Reactors Sulfate elimination Sulfates Temperature Textile wastewater Textiles Waste water Wastewater treatment Wastewaters Water Purification - methods Water treatment and pollution |
| title | Textiles wastewater treatment using anoxic filter bed and biological wriggle bed-ozone biological aerated filter |
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