Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation
Identifieur interne : 000298 ( Istex/Corpus ); précédent : 000297; suivant : 000299Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation
Auteurs : Sheng H. Lin ; Chi M. Lin ; Horng G. LeuSource :
- Water Research [ 0043-1354 ] ; 1998.
Abstract
The present study is to investigate the treatment of surfactant wastewater by the Fenton process. The surfactants considered here were anionic alkylbenzene sulfonate (ABS) and linear alkylbenzene sulfonate (LAS), both being widely used in the household and industrial detergents. Experiments were conducted to examine the effects of pH, amounts of ferrous sulfate (FeSO4) and hydrogen peroxide (H2O2) and temperature on the surfactant removal. Chemical coagulation was also considered as an addition in improving the turbidity and dissolved Fe removal after the Fenton process. A first-order kinetic model was adopted to represent the Fenton oxidation of surfactant wastewater. The relation between the reaction rate coefficient and the ferrous sulfate and hydrogen peroxide concentrations and operating temperature was experimentally established using the test data.
Url:
DOI: 10.1016/S0043-1354(98)00403-5
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<record><TEI wicri:istexFullTextTei="biblStruct"><teiHeader><fileDesc><titleStmt><title>Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation</title><author><name sortKey="Lin, Sheng H" sort="Lin, Sheng H" uniqKey="Lin S" first="Sheng H" last="Lin">Sheng H. Lin</name><affiliation><mods:affiliation>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</mods:affiliation></affiliation><affiliation><mods:affiliation>Author to whom all correspondence should be addressed</mods:affiliation></affiliation></author><author><name sortKey="Lin, Chi M" sort="Lin, Chi M" uniqKey="Lin C" first="Chi M" last="Lin">Chi M. Lin</name><affiliation><mods:affiliation>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</mods:affiliation></affiliation></author><author><name sortKey="Leu, Horng G" sort="Leu, Horng G" uniqKey="Leu H" first="Horng G" last="Leu">Horng G. Leu</name><affiliation><mods:affiliation>Environmental Protection Bureau, Taoyuan County, Taoyuan 330, Taiwan</mods:affiliation></affiliation></author></titleStmt><publicationStmt><idno type="wicri:source">ISTEX</idno><idno type="RBID">ISTEX:FC671518B665BA4EA5FFC55C2515865D58806FFD</idno><date when="1999" year="1999">1999</date><idno type="doi">10.1016/S0043-1354(98)00403-5</idno><idno type="url">https://api.istex.fr/document/FC671518B665BA4EA5FFC55C2515865D58806FFD/fulltext/pdf</idno><idno type="wicri:Area/Istex/Corpus">000298</idno></publicationStmt><sourceDesc><biblStruct><analytic><title level="a">Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation</title><author><name sortKey="Lin, Sheng H" sort="Lin, Sheng H" uniqKey="Lin S" first="Sheng H" last="Lin">Sheng H. Lin</name><affiliation><mods:affiliation>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</mods:affiliation></affiliation><affiliation><mods:affiliation>Author to whom all correspondence should be addressed</mods:affiliation></affiliation></author><author><name sortKey="Lin, Chi M" sort="Lin, Chi M" uniqKey="Lin C" first="Chi M" last="Lin">Chi M. Lin</name><affiliation><mods:affiliation>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</mods:affiliation></affiliation></author><author><name sortKey="Leu, Horng G" sort="Leu, Horng G" uniqKey="Leu H" first="Horng G" last="Leu">Horng G. Leu</name><affiliation><mods:affiliation>Environmental Protection Bureau, Taoyuan County, Taoyuan 330, Taiwan</mods:affiliation></affiliation></author></analytic><monogr></monogr><series><title level="j">Water Research</title><title level="j" type="abbrev">WR</title><idno type="ISSN">0043-1354</idno><imprint><publisher>ELSEVIER</publisher><date type="published" when="1998">1998</date><biblScope unit="volume">33</biblScope><biblScope unit="issue">7</biblScope><biblScope unit="page" from="1735">1735</biblScope><biblScope unit="page" to="1741">1741</biblScope></imprint><idno type="ISSN">0043-1354</idno></series><idno type="istex">FC671518B665BA4EA5FFC55C2515865D58806FFD</idno><idno type="DOI">10.1016/S0043-1354(98)00403-5</idno><idno type="PII">S0043-1354(98)00403-5</idno></biblStruct></sourceDesc><seriesStmt><idno type="ISSN">0043-1354</idno></seriesStmt></fileDesc><profileDesc><textClass></textClass><langUsage><language ident="en">en</language></langUsage></profileDesc></teiHeader><front><div type="abstract" xml:lang="en">The present study is to investigate the treatment of surfactant wastewater by the Fenton process. The surfactants considered here were anionic alkylbenzene sulfonate (ABS) and linear alkylbenzene sulfonate (LAS), both being widely used in the household and industrial detergents. Experiments were conducted to examine the effects of pH, amounts of ferrous sulfate (FeSO4) and hydrogen peroxide (H2O2) and temperature on the surfactant removal. Chemical coagulation was also considered as an addition in improving the turbidity and dissolved Fe removal after the Fenton process. A first-order kinetic model was adopted to represent the Fenton oxidation of surfactant wastewater. The relation between the reaction rate coefficient and the ferrous sulfate and hydrogen peroxide concentrations and operating temperature was experimentally established using the test data.</div></front></TEI><istex><corpusName>elsevier</corpusName><author><json:item><name>Sheng H Lin</name><affiliations><json:string>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</json:string><json:string>Author to whom all correspondence should be addressed</json:string></affiliations></json:item><json:item><name>chi M Lin</name><affiliations><json:string>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</json:string></affiliations></json:item><json:item><name>Horng G Leu</name><affiliations><json:string>Environmental Protection Bureau, Taoyuan County, Taoyuan 330, Taiwan</json:string></affiliations></json:item></author><subject><json:item><lang><json:string>eng</json:string></lang><value>Fenton oxidation</value></json:item><json:item><lang><json:string>eng</json:string></lang><value>surfactant wastewater</value></json:item><json:item><lang><json:string>eng</json:string></lang><value>kinetics</value></json:item><json:item><lang><json:string>eng</json:string></lang><value>chemical coagulation</value></json:item></subject><language><json:string>eng</json:string></language><abstract>The present study is to investigate the treatment of surfactant wastewater by the Fenton process. The surfactants considered here were anionic alkylbenzene sulfonate (ABS) and linear alkylbenzene sulfonate (LAS), both being widely used in the household and industrial detergents. Experiments were conducted to examine the effects of pH, amounts of ferrous sulfate (FeSO4) and hydrogen peroxide (H2O2) and temperature on the surfactant removal. Chemical coagulation was also considered as an addition in improving the turbidity and dissolved Fe removal after the Fenton process. A first-order kinetic model was adopted to represent the Fenton oxidation of surfactant wastewater. The relation between the reaction rate coefficient and the ferrous sulfate and hydrogen peroxide concentrations and operating temperature was experimentally established using the test data.</abstract><qualityIndicators><score>4.497</score><pdfVersion>1.2</pdfVersion><pdfPageSize>595 x 841 pts</pdfPageSize><refBibsNative>true</refBibsNative><keywordCount>4</keywordCount><abstractCharCount>867</abstractCharCount><pdfWordCount>3033</pdfWordCount><pdfCharCount>18345</pdfCharCount><pdfPageCount>7</pdfPageCount><abstractWordCount>122</abstractWordCount></qualityIndicators><title>Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation</title><pii><json:string>S0043-1354(98)00403-5</json:string></pii><genre><json:string>brief communication</json:string></genre><host><volume>33</volume><pii><json:string>S0043-1354(00)X0051-6</json:string></pii><pages><last>1741</last><first>1735</first></pages><issn><json:string>0043-1354</json:string></issn><issue>7</issue><genre></genre><language><json:string>unknown</json:string></language><title>Water Research</title><publicationDate>1999</publicationDate></host><categories><wos><json:string>ENGINEERING, CIVIL</json:string><json:string>ENGINEERING, ENVIRONMENTAL</json:string><json:string>ENVIRONMENTAL SCIENCES</json:string><json:string>WATER RESOURCES</json:string></wos></categories><publicationDate>1998</publicationDate><copyrightDate>1999</copyrightDate><doi><json:string>10.1016/S0043-1354(98)00403-5</json:string></doi><id>FC671518B665BA4EA5FFC55C2515865D58806FFD</id><fulltext><json:item><original>true</original><mimetype>application/pdf</mimetype><extension>pdf</extension><uri>https://api.istex.fr/document/FC671518B665BA4EA5FFC55C2515865D58806FFD/fulltext/pdf</uri></json:item><json:item><original>false</original><mimetype>application/zip</mimetype><extension>zip</extension><uri>https://api.istex.fr/document/FC671518B665BA4EA5FFC55C2515865D58806FFD/fulltext/zip</uri></json:item><istex:fulltextTEI uri="https://api.istex.fr/document/FC671518B665BA4EA5FFC55C2515865D58806FFD/fulltext/tei"><teiHeader><fileDesc><titleStmt><title level="a">Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation</title></titleStmt><publicationStmt><authority>ISTEX</authority><publisher>ELSEVIER</publisher><availability><p>ELSEVIER</p></availability><date>1999</date></publicationStmt><notesStmt><note type="content">Section title: Research Note</note><note type="content">Fig. 1: Experimental schematic.</note><note type="content">Fig. 2: Changes in the residual H2O2 and surfactant concentrations as a function of time with 60mgl−1 [H2O2]0 and 60mgl−1 [FeSO4]0 at 30°C.</note><note type="content">Fig. 3: Effect of [FeSO4]0 on the surfactant removal with 60mgl−1 [H2O2]0 at 30°C without chemical coagulation.</note><note type="content">Fig. 4: Effect of [H2O2]0 on the surfactant removal with 90mgl−1 [FeSO4]0 at 30°C without chemical coagulation.</note><note type="content">Fig. 5: NTU of treated wastewater vs settling time after Fenton oxidation with 60mgl−1 [H2O2]0 and 90mgl−1 [FeSO4]0 at 30°C without chemical coagulation.</note><note type="content">Fig. 6: Effect of [H2O2]0 on the model fit of first-order kinetics with 90mgl−1 [FeSO4]0 without chemical coagulation.</note><note type="content">Fig. 7: Effect of [FeSO4]0 on the model fit of first-order kinetics with 60mgl−1 [H2O2]0 without chemical coagulation.</note><note type="content">Fig. 8: The rate coefficients of Fenton oxidation without chemical coagulation as a function of [H2O2]0 with 90mgl−1 [FeSO4]0 (a) and [FeSO4]0 with 60mgl−1 [H2O2]0 (b).</note><note type="content">Fig. 9: The Arrhenius plots of the rate coefficients of Fenton oxidation without chemical coagulation.</note><note type="content">Table 1: The residual Fe concentration in the treated wastewater</note></notesStmt><sourceDesc><biblStruct type="inbook"><analytic><title level="a">Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation</title><author><persName><forename type="first">Sheng H</forename><surname>Lin</surname></persName><affiliation>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</affiliation><affiliation>Author to whom all correspondence should be addressed</affiliation></author><author><persName><forename type="first">chi M</forename><surname>Lin</surname></persName><affiliation>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</affiliation></author><author><persName><forename type="first">Horng G</forename><surname>Leu</surname></persName><affiliation>Environmental Protection Bureau, Taoyuan County, Taoyuan 330, Taiwan</affiliation></author></analytic><monogr><title level="j">Water Research</title><title level="j" type="abbrev">WR</title><idno type="pISSN">0043-1354</idno><idno type="PII">S0043-1354(00)X0051-6</idno><imprint><publisher>ELSEVIER</publisher><date type="published" when="1998"></date><biblScope unit="volume">33</biblScope><biblScope unit="issue">7</biblScope><biblScope unit="page" from="1735">1735</biblScope><biblScope unit="page" to="1741">1741</biblScope></imprint></monogr><idno type="istex">FC671518B665BA4EA5FFC55C2515865D58806FFD</idno><idno type="DOI">10.1016/S0043-1354(98)00403-5</idno><idno type="PII">S0043-1354(98)00403-5</idno></biblStruct></sourceDesc></fileDesc><profileDesc><creation><date>1999</date></creation><langUsage><language ident="en">en</language></langUsage><abstract xml:lang="en"><p>The present study is to investigate the treatment of surfactant wastewater by the Fenton process. The surfactants considered here were anionic alkylbenzene sulfonate (ABS) and linear alkylbenzene sulfonate (LAS), both being widely used in the household and industrial detergents. Experiments were conducted to examine the effects of pH, amounts of ferrous sulfate (FeSO4) and hydrogen peroxide (H2O2) and temperature on the surfactant removal. Chemical coagulation was also considered as an addition in improving the turbidity and dissolved Fe removal after the Fenton process. A first-order kinetic model was adopted to represent the Fenton oxidation of surfactant wastewater. The relation between the reaction rate coefficient and the ferrous sulfate and hydrogen peroxide concentrations and operating temperature was experimentally established using the test data.</p></abstract><textClass><keywords scheme="keyword"><list><head>Keywords</head><item><term>Fenton oxidation</term></item><item><term>surfactant wastewater</term></item><item><term>kinetics</term></item><item><term>chemical coagulation</term></item></list></keywords></textClass></profileDesc><revisionDesc><change when="1998-09-01">Registration</change><change when="1998">Published</change></revisionDesc></teiHeader></istex:fulltextTEI><json:item><original>false</original><mimetype>text/plain</mimetype><extension>txt</extension><uri>https://api.istex.fr/document/FC671518B665BA4EA5FFC55C2515865D58806FFD/fulltext/txt</uri></json:item></fulltext><metadata><istex:metadataXml wicri:clean="Elsevier, elements deleted: ce:floats; body; tail"><istex:xmlDeclaration>version="1.0" encoding="utf-8"</istex:xmlDeclaration><istex:docType PUBLIC="-//ES//DTD journal article DTD version 4.5.2//EN//XML" URI="art452.dtd" name="istex:docType"><istex:entity SYSTEM="gr1" NDATA="IMAGE" name="gr1"></istex:entity><istex:entity SYSTEM="gr2" NDATA="IMAGE" name="gr2"></istex:entity><istex:entity SYSTEM="gr3" NDATA="IMAGE" name="gr3"></istex:entity><istex:entity SYSTEM="gr4" NDATA="IMAGE" name="gr4"></istex:entity><istex:entity SYSTEM="gr5" NDATA="IMAGE" name="gr5"></istex:entity><istex:entity SYSTEM="gr6" NDATA="IMAGE" name="gr6"></istex:entity><istex:entity SYSTEM="gr7" NDATA="IMAGE" name="gr7"></istex:entity><istex:entity SYSTEM="gr8" NDATA="IMAGE" name="gr8"></istex:entity><istex:entity SYSTEM="gr9" NDATA="IMAGE" name="gr9"></istex:entity></istex:docType><istex:document><converted-article version="4.5.2" docsubtype="sco"><item-info><jid>WR</jid><aid>2094</aid><ce:pii>S0043-1354(98)00403-5</ce:pii><ce:doi>10.1016/S0043-1354(98)00403-5</ce:doi><ce:copyright year="1999" type="full-transfer">Elsevier Science Ltd</ce:copyright></item-info><head><ce:dochead><ce:textfn>Research Note</ce:textfn></ce:dochead><ce:title>Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation</ce:title><ce:author-group><ce:author><ce:given-name>Sheng H</ce:given-name><ce:surname>Lin</ce:surname><ce:cross-ref refid="AFF1">a</ce:cross-ref><ce:cross-ref refid="CORR1">*</ce:cross-ref></ce:author><ce:author><ce:given-name>chi M</ce:given-name><ce:surname>Lin</ce:surname><ce:cross-ref refid="AFF1">a</ce:cross-ref></ce:author><ce:author><ce:given-name>Horng G</ce:given-name><ce:surname>Leu</ce:surname><ce:cross-ref refid="AFF2">b</ce:cross-ref></ce:author><ce:affiliation id="AFF1"><ce:label>a</ce:label><ce:textfn>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</ce:textfn></ce:affiliation><ce:affiliation id="AFF2"><ce:label>b</ce:label><ce:textfn>Environmental Protection Bureau, Taoyuan County, Taoyuan 330, Taiwan</ce:textfn></ce:affiliation><ce:correspondence id="CORR1"><ce:label>*</ce:label><ce:text>Author to whom all correspondence should be addressed</ce:text></ce:correspondence></ce:author-group><ce:date-received day="1" month="1" year="1998"></ce:date-received><ce:date-accepted day="1" month="9" year="1998"></ce:date-accepted><ce:abstract><ce:section-title>Abstract</ce:section-title><ce:abstract-sec><ce:simple-para>The present study is to investigate the treatment of surfactant wastewater by the Fenton process. The surfactants considered here were anionic alkylbenzene sulfonate (ABS) and linear alkylbenzene sulfonate (LAS), both being widely used in the household and industrial detergents. Experiments were conducted to examine the effects of pH, amounts of ferrous sulfate (FeSO<ce:inf>4</ce:inf>) and hydrogen peroxide (H<ce:inf>2</ce:inf>O<ce:inf>2</ce:inf>) and temperature on the surfactant removal. Chemical coagulation was also considered as an addition in improving the turbidity and dissolved Fe removal after the Fenton process. A first-order kinetic model was adopted to represent the Fenton oxidation of surfactant wastewater. The relation between the reaction rate coefficient and the ferrous sulfate and hydrogen peroxide concentrations and operating temperature was experimentally established using the test data.</ce:simple-para></ce:abstract-sec></ce:abstract><ce:keywords class="keyword"><ce:section-title>Keywords</ce:section-title><ce:keyword><ce:text>Fenton oxidation</ce:text></ce:keyword><ce:keyword><ce:text>surfactant wastewater</ce:text></ce:keyword><ce:keyword><ce:text>kinetics</ce:text></ce:keyword><ce:keyword><ce:text>chemical coagulation</ce:text></ce:keyword></ce:keywords></head></converted-article></istex:document></istex:metadataXml><mods version="3.6"><titleInfo><title>Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation</title></titleInfo><titleInfo type="alternative" contentType="CDATA"><title>Operating characteristics and kinetic studies of surfactant wastewater treatment by Fenton oxidation</title></titleInfo><name type="personal"><namePart type="given">Sheng H</namePart><namePart type="family">Lin</namePart><affiliation>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</affiliation><affiliation>Author to whom all correspondence should be addressed</affiliation><role><roleTerm type="text">author</roleTerm></role></name><name type="personal"><namePart type="given">chi M</namePart><namePart type="family">Lin</namePart><affiliation>Department of Chemical Engineering, Yuan Ze University, Neili, Taoyuan 320, Taiwan</affiliation><role><roleTerm type="text">author</roleTerm></role></name><name type="personal"><namePart type="given">Horng G</namePart><namePart type="family">Leu</namePart><affiliation>Environmental Protection Bureau, Taoyuan County, Taoyuan 330, Taiwan</affiliation><role><roleTerm type="text">author</roleTerm></role></name><typeOfResource>text</typeOfResource><genre type="brief communication" displayLabel="Short communication"></genre><originInfo><publisher>ELSEVIER</publisher><dateIssued encoding="w3cdtf">1998</dateIssued><dateValid encoding="w3cdtf">1998-09-01</dateValid><copyrightDate encoding="w3cdtf">1999</copyrightDate></originInfo><language><languageTerm type="code" authority="iso639-2b">eng</languageTerm><languageTerm type="code" authority="rfc3066">en</languageTerm></language><physicalDescription><internetMediaType>text/html</internetMediaType></physicalDescription><abstract lang="en">The present study is to investigate the treatment of surfactant wastewater by the Fenton process. The surfactants considered here were anionic alkylbenzene sulfonate (ABS) and linear alkylbenzene sulfonate (LAS), both being widely used in the household and industrial detergents. Experiments were conducted to examine the effects of pH, amounts of ferrous sulfate (FeSO4) and hydrogen peroxide (H2O2) and temperature on the surfactant removal. Chemical coagulation was also considered as an addition in improving the turbidity and dissolved Fe removal after the Fenton process. A first-order kinetic model was adopted to represent the Fenton oxidation of surfactant wastewater. The relation between the reaction rate coefficient and the ferrous sulfate and hydrogen peroxide concentrations and operating temperature was experimentally established using the test data.</abstract><note type="content">Section title: Research Note</note><note type="content">Fig. 1: Experimental schematic.</note><note type="content">Fig. 2: Changes in the residual H2O2 and surfactant concentrations as a function of time with 60mgl−1 [H2O2]0 and 60mgl−1 [FeSO4]0 at 30°C.</note><note type="content">Fig. 3: Effect of [FeSO4]0 on the surfactant removal with 60mgl−1 [H2O2]0 at 30°C without chemical coagulation.</note><note type="content">Fig. 4: Effect of [H2O2]0 on the surfactant removal with 90mgl−1 [FeSO4]0 at 30°C without chemical coagulation.</note><note type="content">Fig. 5: NTU of treated wastewater vs settling time after Fenton oxidation with 60mgl−1 [H2O2]0 and 90mgl−1 [FeSO4]0 at 30°C without chemical coagulation.</note><note type="content">Fig. 6: Effect of [H2O2]0 on the model fit of first-order kinetics with 90mgl−1 [FeSO4]0 without chemical coagulation.</note><note type="content">Fig. 7: Effect of [FeSO4]0 on the model fit of first-order kinetics with 60mgl−1 [H2O2]0 without chemical coagulation.</note><note type="content">Fig. 8: The rate coefficients of Fenton oxidation without chemical coagulation as a function of [H2O2]0 with 90mgl−1 [FeSO4]0 (a) and [FeSO4]0 with 60mgl−1 [H2O2]0 (b).</note><note type="content">Fig. 9: The Arrhenius plots of the rate coefficients of Fenton oxidation without chemical coagulation.</note><note type="content">Table 1: The residual Fe concentration in the treated wastewater</note><subject><genre>Keywords</genre><topic>Fenton oxidation</topic><topic>surfactant wastewater</topic><topic>kinetics</topic><topic>chemical coagulation</topic></subject><relatedItem type="host"><titleInfo><title>Water Research</title></titleInfo><titleInfo type="abbreviated"><title>WR</title></titleInfo><genre type="Journal">journal</genre><originInfo><dateIssued encoding="w3cdtf">199905</dateIssued></originInfo><identifier type="ISSN">0043-1354</identifier><identifier type="PII">S0043-1354(00)X0051-6</identifier><part><date>199905</date><detail type="volume"><number>33</number><caption>vol.</caption></detail><detail type="issue"><number>7</number><caption>no.</caption></detail><extent unit="issue pages"><start>1559</start><end>1760</end></extent><extent unit="pages"><start>1735</start><end>1741</end></extent></part></relatedItem><identifier type="istex">FC671518B665BA4EA5FFC55C2515865D58806FFD</identifier><identifier type="DOI">10.1016/S0043-1354(98)00403-5</identifier><identifier type="PII">S0043-1354(98)00403-5</identifier><accessCondition type="use and reproduction" contentType="">© 1999Elsevier Science Ltd</accessCondition><recordInfo><recordContentSource>ELSEVIER</recordContentSource><recordOrigin>Elsevier Science Ltd, ©1999</recordOrigin></recordInfo></mods></metadata><enrichments><istex:catWosTEI uri="https://api.istex.fr/document/FC671518B665BA4EA5FFC55C2515865D58806FFD/enrichments/catWos"><teiHeader><profileDesc><textClass><classCode scheme="WOS">ENGINEERING, CIVIL</classCode><classCode scheme="WOS">ENGINEERING, ENVIRONMENTAL</classCode><classCode scheme="WOS">ENVIRONMENTAL SCIENCES</classCode><classCode scheme="WOS">WATER RESOURCES</classCode></textClass></profileDesc></teiHeader></istex:catWosTEI></enrichments><serie></serie></istex></record>Pour manipuler ce document sous Unix (Dilib)
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