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The Removal of Chlorinated Organics from Conventional Pulp and Paper Wastewater Treatment Systems
Removals of adsorbable organic halides (AOX) achieved by 8 full-scale wastewater treatment systems at pulp mills in North America were surveyed over a 2-year period. AOX removals averaged 46 per cent for activated sludge systems and 34 per cent for aerated stabilization systems studied. The best per...
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Published in: | Water science and technology 1992, Vol.26 (1-2), p.417-425 |
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creator | Bryant, C W Avenell, J J Barkley, W A Thut, R N |
description | Removals of adsorbable organic halides (AOX) achieved by 8 full-scale wastewater treatment systems at pulp mills in North America were surveyed over a 2-year period. AOX removals averaged 46 per cent for activated sludge systems and 34 per cent for aerated stabilization systems studied. The best performance was recorded at a sulphite mill activated sludge system which consistently removed 53 per cent of total AOX and 62 per cent of low-molecular-weight AOX in bleaching wastewaters. In some cases, the use of oxygen and peroxide and chlorine dioxide substitution reduced influent AOX loadings, with little effect on treatment plant removal efficiency. |
doi_str_mv | 10.2166/wst.1992.0421 |
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(eds.) ; Suzuki, M</contributor><creatorcontrib>Bryant, C W ; Avenell, J J ; Barkley, W A ; Thut, R N ; et al. (eds.) ; Suzuki, M</creatorcontrib><description>Removals of adsorbable organic halides (AOX) achieved by 8 full-scale wastewater treatment systems at pulp mills in North America were surveyed over a 2-year period. AOX removals averaged 46 per cent for activated sludge systems and 34 per cent for aerated stabilization systems studied. The best performance was recorded at a sulphite mill activated sludge system which consistently removed 53 per cent of total AOX and 62 per cent of low-molecular-weight AOX in bleaching wastewaters. In some cases, the use of oxygen and peroxide and chlorine dioxide substitution reduced influent AOX loadings, with little effect on treatment plant removal efficiency.</description><identifier>ISSN: 0273-1223</identifier><identifier>EISSN: 1996-9732</identifier><identifier>DOI: 10.2166/wst.1992.0421</identifier><language>eng</language><publisher>London: IWA Publishing</publisher><subject>Activated sludge ; Aeration ; Basins ; Bleaching ; Bleaching wastes ; Chlorination ; Chlorine ; Chlorine dioxide ; Influents ; Molecular weight ; Peroxide ; Plant removal ; Pulp & paper industry ; Pulp & paper mills ; Pulp mill effluents ; Removal ; Sludge ; Sludge treatment ; Sulfite ; Surveying ; Wastewater ; Wastewater treatment ; Water treatment plants ; Weight</subject><ispartof>Water science and technology, 1992, Vol.26 (1-2), p.417-425</ispartof><rights>Copyright IWA Publishing Jul 1992</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c333t-27cdcb3ec00aaf5aff243116ce85ccd16fc49ebd515fe6b93470c83a92d1a39f3</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>309,310,314,780,784,789,790,4024,4050,4051,23930,23931,25140,27923,27924,27925</link.rule.ids></links><search><contributor>et al. 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In some cases, the use of oxygen and peroxide and chlorine dioxide substitution reduced influent AOX loadings, with little effect on treatment plant removal efficiency.</description><subject>Activated sludge</subject><subject>Aeration</subject><subject>Basins</subject><subject>Bleaching</subject><subject>Bleaching wastes</subject><subject>Chlorination</subject><subject>Chlorine</subject><subject>Chlorine dioxide</subject><subject>Influents</subject><subject>Molecular weight</subject><subject>Peroxide</subject><subject>Plant removal</subject><subject>Pulp & paper industry</subject><subject>Pulp & paper mills</subject><subject>Pulp mill effluents</subject><subject>Removal</subject><subject>Sludge</subject><subject>Sludge treatment</subject><subject>Sulfite</subject><subject>Surveying</subject><subject>Wastewater</subject><subject>Wastewater treatment</subject><subject>Water treatment plants</subject><subject>Weight</subject><issn>0273-1223</issn><issn>1996-9732</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1992</creationdate><recordtype>article</recordtype><recordid>eNqN0s1LwzAYBvAgCs7p0XtA8NaZ5G3T5ijFLxg4dOKxZGniOtqmJu3G_ntT5snLPCWEX154Hx6ErimZMcr53c73MyoEm5GY0RM0CXceiRTYKZoQlkJEGYNzdOH9hhCSQkwmSC7XGr_pxm5lja3B-bq2rmplr0v86r5kWymPjbMNzm271W1f2TbIxVB3WLYlXshOO_wpfa934ZPDS6dl3wSI3_fhsfGX6MzI2uur33OKPh4flvlzNH99esnv55ECgD5iqSrVCrQiREqTSGNYDJRypbNEqZJyo2KhV2VCE6P5SkCcEpWBFKykEoSBKbo9zO2c_R6074um8krXtWy1HXzBQjLAefIPyAVkghyHkMYs4cch5TEjjLPjEFJCmcgCvPkDN3ZwIflgRMglTTIybhIdlHLWe6dN0bmqkW5fUFKMlShCJYqxEsVYCfgBIfep6A</recordid><startdate>1992</startdate><enddate>1992</enddate><creator>Bryant, C W</creator><creator>Avenell, J J</creator><creator>Barkley, W A</creator><creator>Thut, R N</creator><general>IWA Publishing</general><scope>AAYXX</scope><scope>CITATION</scope><scope>3V.</scope><scope>7QH</scope><scope>7UA</scope><scope>7X7</scope><scope>7XB</scope><scope>88E</scope><scope>8FE</scope><scope>8FG</scope><scope>8FI</scope><scope>8FJ</scope><scope>8FK</scope><scope>ABJCF</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>BHPHI</scope><scope>BKSAR</scope><scope>C1K</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>F1W</scope><scope>FYUFA</scope><scope>GHDGH</scope><scope>H96</scope><scope>H97</scope><scope>HCIFZ</scope><scope>K9.</scope><scope>L.G</scope><scope>L6V</scope><scope>M0S</scope><scope>M1P</scope><scope>M7S</scope><scope>PCBAR</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PTHSS</scope><scope>7T7</scope><scope>7TV</scope><scope>8FD</scope><scope>FR3</scope><scope>P64</scope><scope>7SC</scope><scope>JQ2</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>7TB</scope><scope>KR7</scope></search><sort><creationdate>1992</creationdate><title>The Removal of Chlorinated Organics from Conventional Pulp and Paper Wastewater Treatment Systems</title><author>Bryant, C W ; 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(eds.)</au><au>Suzuki, M</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>The Removal of Chlorinated Organics from Conventional Pulp and Paper Wastewater Treatment Systems</atitle><jtitle>Water science and technology</jtitle><date>1992</date><risdate>1992</risdate><volume>26</volume><issue>1-2</issue><spage>417</spage><epage>425</epage><pages>417-425</pages><issn>0273-1223</issn><eissn>1996-9732</eissn><abstract>Removals of adsorbable organic halides (AOX) achieved by 8 full-scale wastewater treatment systems at pulp mills in North America were surveyed over a 2-year period. AOX removals averaged 46 per cent for activated sludge systems and 34 per cent for aerated stabilization systems studied. The best performance was recorded at a sulphite mill activated sludge system which consistently removed 53 per cent of total AOX and 62 per cent of low-molecular-weight AOX in bleaching wastewaters. In some cases, the use of oxygen and peroxide and chlorine dioxide substitution reduced influent AOX loadings, with little effect on treatment plant removal efficiency.</abstract><cop>London</cop><pub>IWA Publishing</pub><doi>10.2166/wst.1992.0421</doi><tpages>9</tpages></addata></record> |
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source | Alma/SFX Local Collection |
subjects | Activated sludge Aeration Basins Bleaching Bleaching wastes Chlorination Chlorine Chlorine dioxide Influents Molecular weight Peroxide Plant removal Pulp & paper industry Pulp & paper mills Pulp mill effluents Removal Sludge Sludge treatment Sulfite Surveying Wastewater Wastewater treatment Water treatment plants Weight |
title | The Removal of Chlorinated Organics from Conventional Pulp and Paper Wastewater Treatment Systems |
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