Gas–liquid mass transfer in an airlift reactor — analytical solution and experimental confirmation
Identifieur interne : 000738 ( Istex/Corpus ); précédent : 000737; suivant : 000739Gas–liquid mass transfer in an airlift reactor — analytical solution and experimental confirmation
Auteurs : Hatem Dhaouadi ; Souhila Poncin ; Noël Midoux ; Gabriel WildSource :
- Chemical Engineering & Processing: Process Intensification [ 0255-2701 ] ; 2001.
English descriptors
- KwdEn :
- Airlift, Airlift reactor, Airlift reactors, Analytical solution, Axial dispersion, Basic equations, Chemical engineering, Complete model, Dhaouadi, Dimensionless, Downcomer, Dynamic method, Elsevier science, External loop airlift reactor, Laplace, Liquid circulation, Liquid mass transfer, Mass transfer, Oxygen concentration, Oxygen probe, Riser, Same reactor, Sophisticated model, Static pressure, Volumetric mass transfer.
- Teeft :
- Airlift, Airlift reactor, Airlift reactors, Analytical solution, Axial dispersion, Basic equations, Chemical engineering, Complete model, Dhaouadi, Dimensionless, Downcomer, Dynamic method, Elsevier science, External loop airlift reactor, Laplace, Liquid circulation, Liquid mass transfer, Mass transfer, Oxygen concentration, Oxygen probe, Riser, Same reactor, Sophisticated model, Static pressure, Volumetric mass transfer.
Abstract
Abstract: Gas–liquid mass transfer behavior in an external loop airlift reactor is investigated. The riser and the downcomer of 6 m height have a diameter of 0.15 and 0.08 m, respectively. The classical ‘gassing out’ dynamic method is used to obtain the evolution with time of dissolved oxygen concentration profiles. An analytical description of the concentration profiles with time following the switch in the inlet gas concentration is presented and allows the evaluation of the gas–liquid mass transfer coefficient for the different gas velocities used. The comparison between the values of kLa determined from this simplified model and those obtained in the same reactor from a more complete and sophisticated model shows a good agreement.
Url:
DOI: 10.1016/S0255-2701(00)00132-X
Links to Exploration step
ISTEX:528E6054FC6FECF5356EEC304ADCC8838D9A7CD5Le document en format XML
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France</mods:affiliation></affiliation></author></analytic><monogr></monogr><series><title level="j">Chemical Engineering & Processing: Process Intensification</title><title level="j" type="abbrev">CEP</title><idno type="ISSN">0255-2701</idno><imprint><publisher>ELSEVIER</publisher><date type="published" when="2001">2001</date><biblScope unit="volume">40</biblScope><biblScope unit="issue">2</biblScope><biblScope unit="page" from="129">129</biblScope><biblScope unit="page" to="133">133</biblScope></imprint><idno type="ISSN">0255-2701</idno></series></biblStruct></sourceDesc><seriesStmt><idno type="ISSN">0255-2701</idno></seriesStmt></fileDesc><profileDesc><textClass><keywords scheme="KwdEn" xml:lang="en"><term>Airlift</term><term>Airlift reactor</term><term>Airlift reactors</term><term>Analytical solution</term><term>Axial dispersion</term><term>Basic equations</term><term>Chemical engineering</term><term>Complete model</term><term>Dhaouadi</term><term>Dimensionless</term><term>Downcomer</term><term>Dynamic method</term><term>Elsevier science</term><term>External loop airlift reactor</term><term>Laplace</term><term>Liquid circulation</term><term>Liquid mass transfer</term><term>Mass transfer</term><term>Oxygen concentration</term><term>Oxygen probe</term><term>Riser</term><term>Same reactor</term><term>Sophisticated model</term><term>Static pressure</term><term>Volumetric mass transfer</term></keywords><keywords scheme="Teeft" xml:lang="en"><term>Airlift</term><term>Airlift reactor</term><term>Airlift reactors</term><term>Analytical solution</term><term>Axial dispersion</term><term>Basic equations</term><term>Chemical engineering</term><term>Complete model</term><term>Dhaouadi</term><term>Dimensionless</term><term>Downcomer</term><term>Dynamic method</term><term>Elsevier science</term><term>External loop airlift reactor</term><term>Laplace</term><term>Liquid circulation</term><term>Liquid mass transfer</term><term>Mass transfer</term><term>Oxygen concentration</term><term>Oxygen probe</term><term>Riser</term><term>Same reactor</term><term>Sophisticated model</term><term>Static pressure</term><term>Volumetric mass transfer</term></keywords></textClass><langUsage><language ident="en">en</language></langUsage></profileDesc></teiHeader><front><div type="abstract" xml:lang="en">Abstract: Gas–liquid mass transfer behavior in an external loop airlift reactor is investigated. The riser and the downcomer of 6 m height have a diameter of 0.15 and 0.08 m, respectively. The classical ‘gassing out’ dynamic method is used to obtain the evolution with time of dissolved oxygen concentration profiles. An analytical description of the concentration profiles with time following the switch in the inlet gas concentration is presented and allows the evaluation of the gas–liquid mass transfer coefficient for the different gas velocities used. The comparison between the values of kLa determined from this simplified model and those obtained in the same reactor from a more complete and sophisticated model shows a good agreement.</div></front></TEI><istex><corpusName>elsevier</corpusName><keywords><teeft><json:string>riser</json:string><json:string>dhaouadi</json:string><json:string>airlift</json:string><json:string>downcomer</json:string><json:string>analytical solution</json:string><json:string>dimensionless</json:string><json:string>chemical engineering</json:string><json:string>external loop airlift reactor</json:string><json:string>airlift reactor</json:string><json:string>liquid mass transfer</json:string><json:string>mass transfer</json:string><json:string>airlift reactors</json:string><json:string>elsevier science</json:string><json:string>dynamic method</json:string><json:string>oxygen concentration</json:string><json:string>liquid circulation</json:string><json:string>same reactor</json:string><json:string>axial dispersion</json:string><json:string>basic equations</json:string><json:string>static pressure</json:string><json:string>volumetric mass transfer</json:string><json:string>oxygen probe</json:string><json:string>complete model</json:string><json:string>sophisticated model</json:string><json:string>laplace</json:string></teeft></keywords><author><json:item><name>Hatem Dhaouadi</name><affiliations><json:string>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</json:string></affiliations></json:item><json:item><name>Souhila Poncin</name><affiliations><json:string>E-mail: Souhila.Poncin@ensic.inpl-nancy.fr</json:string><json:string>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</json:string></affiliations></json:item><json:item><name>Noël Midoux</name><affiliations><json:string>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</json:string></affiliations></json:item><json:item><name>Gabriel Wild</name><affiliations><json:string>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</json:string></affiliations></json:item></author><subject><json:item><lang><json:string>eng</json:string></lang><value>Airlift</value></json:item><json:item><lang><json:string>eng</json:string></lang><value>Mass transfer</value></json:item><json:item><lang><json:string>eng</json:string></lang><value>Analytical solution</value></json:item></subject><language><json:string>eng</json:string></language><originalGenre><json:string>Full-length article</json:string></originalGenre><abstract>Gas–liquid mass transfer behavior in an external loop airlift reactor is investigated. The riser and the downcomer of 6 m height have a diameter of 0.15 and 0.08 m, respectively. The classical ‘gassing out’ dynamic method is used to obtain the evolution with time of dissolved oxygen concentration profiles. An analytical description of the concentration profiles with time following the switch in the inlet gas concentration is presented and allows the evaluation of the gas–liquid mass transfer coefficient for the different gas velocities used. The comparison between the values of kLa determined from this simplified model and those obtained in the same reactor from a more complete and sophisticated model shows a good agreement.</abstract><qualityIndicators><score>3.204</score><pdfVersion>1.2</pdfVersion><pdfPageSize>552 x 768 pts</pdfPageSize><refBibsNative>true</refBibsNative><keywordCount>3</keywordCount><abstractCharCount>734</abstractCharCount><pdfWordCount>1836</pdfWordCount><pdfCharCount>10480</pdfCharCount><pdfPageCount>5</pdfPageCount><abstractWordCount>114</abstractWordCount></qualityIndicators><title>Gas–liquid mass transfer in an airlift reactor — analytical solution and experimental confirmation</title><pii><json:string>S0255-2701(00)00132-X</json:string></pii><genre><json:string>research-article</json:string></genre><host><title>Chemical Engineering & Processing: Process Intensification</title><language><json:string>unknown</json:string></language><publicationDate>2001</publicationDate><issn><json:string>0255-2701</json:string></issn><pii><json:string>S0255-2701(00)X0022-0</json:string></pii><volume>40</volume><issue>2</issue><pages><first>129</first><last>133</last></pages><genre><json:string>journal</json:string></genre></host><categories><wos><json:string>science</json:string><json:string>engineering, chemical</json:string><json:string>energy & fuels</json:string></wos><scienceMetrix><json:string>applied sciences</json:string><json:string>engineering</json:string><json:string>chemical engineering</json:string></scienceMetrix><inist><json:string>sciences appliquees, technologies et medecines</json:string><json:string>sciences exactes et technologie</json:string><json:string>sciences appliquees</json:string><json:string>pollution</json:string></inist></categories><publicationDate>2001</publicationDate><copyrightDate>2001</copyrightDate><doi><json:string>10.1016/S0255-2701(00)00132-X</json:string></doi><id>528E6054FC6FECF5356EEC304ADCC8838D9A7CD5</id><score>1</score><fulltext><json:item><extension>pdf</extension><original>true</original><mimetype>application/pdf</mimetype><uri>https://api.istex.fr/document/528E6054FC6FECF5356EEC304ADCC8838D9A7CD5/fulltext/pdf</uri></json:item><json:item><extension>zip</extension><original>false</original><mimetype>application/zip</mimetype><uri>https://api.istex.fr/document/528E6054FC6FECF5356EEC304ADCC8838D9A7CD5/fulltext/zip</uri></json:item><istex:fulltextTEI uri="https://api.istex.fr/document/528E6054FC6FECF5356EEC304ADCC8838D9A7CD5/fulltext/tei"><teiHeader><fileDesc><titleStmt><title level="a" type="main" xml:lang="en">Gas–liquid mass transfer in an airlift reactor — analytical solution and experimental confirmation</title></titleStmt><publicationStmt><authority>ISTEX</authority><publisher>ELSEVIER</publisher><availability><p>©2001 Elsevier Science B.V.</p></availability><date>2001</date></publicationStmt><notesStmt><note type="content">Fig. 1: Elementary models used for mass transfer description in the external loop airlift reactor, (a) complete model [3]; (b) simplified model used here.</note><note type="content">Fig. 2: Experimental to analytical solution adjustment for a given axial position in the riser (uG=0.057 m s−1).</note><note type="content">Fig. 3: Comparison between values of kLa obtained by the analytic solution and the numerical solution (complete model, see [3]).</note></notesStmt><sourceDesc><biblStruct type="inbook"><analytic><title level="a" type="main" xml:lang="en">Gas–liquid mass transfer in an airlift reactor — analytical solution and experimental confirmation</title><author xml:id="author-0000"><persName><forename type="first">Hatem</forename><surname>Dhaouadi</surname></persName><affiliation>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</affiliation></author><author xml:id="author-0001"><persName><forename type="first">Souhila</forename><surname>Poncin</surname></persName><email>Souhila.Poncin@ensic.inpl-nancy.fr</email><note type="correspondence"><p>Corresponding author. Tel.: +33-83-175223; fax: +33-83-322975</p></note><affiliation>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</affiliation></author><author xml:id="author-0002"><persName><forename type="first">Noël</forename><surname>Midoux</surname></persName><affiliation>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</affiliation></author><author xml:id="author-0003"><persName><forename type="first">Gabriel</forename><surname>Wild</surname></persName><affiliation>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</affiliation></author><idno type="istex">528E6054FC6FECF5356EEC304ADCC8838D9A7CD5</idno><idno type="DOI">10.1016/S0255-2701(00)00132-X</idno><idno type="PII">S0255-2701(00)00132-X</idno></analytic><monogr><title level="j">Chemical Engineering & Processing: Process Intensification</title><title level="j" type="abbrev">CEP</title><idno type="pISSN">0255-2701</idno><idno type="PII">S0255-2701(00)X0022-0</idno><imprint><publisher>ELSEVIER</publisher><date type="published" when="2001"></date><biblScope unit="volume">40</biblScope><biblScope unit="issue">2</biblScope><biblScope unit="page" from="129">129</biblScope><biblScope unit="page" to="133">133</biblScope></imprint></monogr></biblStruct></sourceDesc></fileDesc><profileDesc><creation><date>2001</date></creation><langUsage><language ident="en">en</language></langUsage><abstract xml:lang="en"><p>Gas–liquid mass transfer behavior in an external loop airlift reactor is investigated. The riser and the downcomer of 6 m height have a diameter of 0.15 and 0.08 m, respectively. The classical ‘gassing out’ dynamic method is used to obtain the evolution with time of dissolved oxygen concentration profiles. An analytical description of the concentration profiles with time following the switch in the inlet gas concentration is presented and allows the evaluation of the gas–liquid mass transfer coefficient for the different gas velocities used. The comparison between the values of kLa determined from this simplified model and those obtained in the same reactor from a more complete and sophisticated model shows a good agreement.</p></abstract><textClass xml:lang="en"><keywords scheme="keyword"><list><head>Keywords</head><item><term>Airlift</term></item><item><term>Mass transfer</term></item><item><term>Analytical solution</term></item></list></keywords></textClass></profileDesc><revisionDesc><change when="2000-01-15">Modified</change><change when="2001">Published</change></revisionDesc></teiHeader></istex:fulltextTEI><json:item><extension>txt</extension><original>false</original><mimetype>text/plain</mimetype><uri>https://api.istex.fr/document/528E6054FC6FECF5356EEC304ADCC8838D9A7CD5/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:docType><istex:document><converted-article version="4.5.2" docsubtype="fla" xml:lang="en"><item-info><jid>CEP</jid><aid>4449</aid><ce:pii>S0255-2701(00)00132-X</ce:pii><ce:doi>10.1016/S0255-2701(00)00132-X</ce:doi><ce:copyright type="full-transfer" year="2001">Elsevier Science B.V.</ce:copyright></item-info><head><ce:title>Gas–liquid mass transfer in an airlift reactor — analytical solution and experimental confirmation</ce:title><ce:author-group><ce:author><ce:given-name>Hatem</ce:given-name><ce:surname>Dhaouadi</ce:surname><ce:cross-ref refid="AFF1"><ce:sup>a</ce:sup></ce:cross-ref><ce:cross-ref refid="AFF2"><ce:sup>b</ce:sup></ce:cross-ref></ce:author><ce:author><ce:given-name>Souhila</ce:given-name><ce:surname>Poncin</ce:surname><ce:cross-ref refid="AFF1"><ce:sup>a</ce:sup></ce:cross-ref><ce:cross-ref refid="CORR1">*</ce:cross-ref><ce:e-address>Souhila.Poncin@ensic.inpl-nancy.fr</ce:e-address></ce:author><ce:author><ce:given-name>Noël</ce:given-name><ce:surname>Midoux</ce:surname><ce:cross-ref refid="AFF1"><ce:sup>a</ce:sup></ce:cross-ref></ce:author><ce:author><ce:given-name>Gabriel</ce:given-name><ce:surname>Wild</ce:surname><ce:cross-ref refid="AFF1"><ce:sup>a</ce:sup></ce:cross-ref></ce:author><ce:affiliation id="AFF1"><ce:label>a</ce:label><ce:textfn>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</ce:textfn></ce:affiliation><ce:affiliation id="AFF2"><ce:label>b</ce:label><ce:textfn>Faculté des Sciences de Monastir, département de Chimie, Tunisie</ce:textfn></ce:affiliation><ce:correspondence id="CORR1"><ce:label>*</ce:label><ce:text>Corresponding author. Tel.: +33-83-175223; fax: +33-83-322975</ce:text></ce:correspondence></ce:author-group><ce:date-received day="15" month="7" year="1999"></ce:date-received><ce:date-revised day="15" month="1" year="2000"></ce:date-revised><ce:date-accepted day="31" month="5" year="2000"></ce:date-accepted><ce:abstract><ce:section-title>Abstract</ce:section-title><ce:abstract-sec><ce:simple-para>Gas–liquid mass transfer behavior in an external loop airlift reactor is investigated. The riser and the downcomer of 6 m height have a diameter of 0.15 and 0.08 m, respectively. The classical ‘gassing out’ dynamic method is used to obtain the evolution with time of dissolved oxygen concentration profiles. An analytical description of the concentration profiles with time following the switch in the inlet gas concentration is presented and allows the evaluation of the gas–liquid mass transfer coefficient for the different gas velocities used. The comparison between the values of <ce:italic>k</ce:italic><ce:inf>L</ce:inf><ce:italic>a</ce:italic> determined from this simplified model and those obtained in the same reactor from a more complete and sophisticated model shows a good agreement.</ce:simple-para></ce:abstract-sec></ce:abstract><ce:keywords class="keyword"><ce:section-title>Keywords</ce:section-title><ce:keyword><ce:text>Airlift</ce:text></ce:keyword><ce:keyword><ce:text>Mass transfer</ce:text></ce:keyword><ce:keyword><ce:text>Analytical solution</ce:text></ce:keyword></ce:keywords></head></converted-article></istex:document></istex:metadataXml><mods version="3.6"><titleInfo lang="en"><title>Gas–liquid mass transfer in an airlift reactor — analytical solution and experimental confirmation</title></titleInfo><titleInfo type="alternative" lang="en" contentType="CDATA"><title>Gas–liquid mass transfer in an airlift reactor — analytical solution and experimental confirmation</title></titleInfo><name type="personal"><namePart type="given">Hatem</namePart><namePart type="family">Dhaouadi</namePart><affiliation>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</affiliation><role><roleTerm type="text">author</roleTerm></role></name><name type="personal"><namePart type="given">Souhila</namePart><namePart type="family">Poncin</namePart><affiliation>E-mail: Souhila.Poncin@ensic.inpl-nancy.fr</affiliation><affiliation>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</affiliation><description>Corresponding author. Tel.: +33-83-175223; fax: +33-83-322975</description><role><roleTerm type="text">author</roleTerm></role></name><name type="personal"><namePart type="given">Noël</namePart><namePart type="family">Midoux</namePart><affiliation>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</affiliation><role><roleTerm type="text">author</roleTerm></role></name><name type="personal"><namePart type="given">Gabriel</namePart><namePart type="family">Wild</namePart><affiliation>Laboratoire des Sciences du Génie Chimique, Ctr Nat de la Recherche Scientifique (CNRS)-ENSIC, BP 451-1 rue Grandville, 54001 Nancy, Cedex, France</affiliation><role><roleTerm type="text">author</roleTerm></role></name><typeOfResource>text</typeOfResource><genre type="research-article" displayLabel="Full-length article" authority="ISTEX" authorityURI="https://content-type.data.istex.fr" valueURI="https://content-type.data.istex.fr/ark:/67375/XTP-1JC4F85T-7">research-article</genre><originInfo><publisher>ELSEVIER</publisher><dateIssued encoding="w3cdtf">2001</dateIssued><dateModified encoding="w3cdtf">2000-01-15</dateModified><copyrightDate encoding="w3cdtf">2001</copyrightDate></originInfo><language><languageTerm type="code" authority="iso639-2b">eng</languageTerm><languageTerm type="code" authority="rfc3066">en</languageTerm></language><abstract lang="en">Abstract: Gas–liquid mass transfer behavior in an external loop airlift reactor is investigated. The riser and the downcomer of 6 m height have a diameter of 0.15 and 0.08 m, respectively. The classical ‘gassing out’ dynamic method is used to obtain the evolution with time of dissolved oxygen concentration profiles. An analytical description of the concentration profiles with time following the switch in the inlet gas concentration is presented and allows the evaluation of the gas–liquid mass transfer coefficient for the different gas velocities used. The comparison between the values of kLa determined from this simplified model and those obtained in the same reactor from a more complete and sophisticated model shows a good agreement.</abstract><note type="content">Fig. 1: Elementary models used for mass transfer description in the external loop airlift reactor, (a) complete model [3]; (b) simplified model used here.</note><note type="content">Fig. 2: Experimental to analytical solution adjustment for a given axial position in the riser (uG=0.057 m s−1).</note><note type="content">Fig. 3: Comparison between values of kLa obtained by the analytic solution and the numerical solution (complete model, see [3]).</note><subject lang="en"><genre>Keywords</genre><topic>Airlift</topic><topic>Mass transfer</topic><topic>Analytical solution</topic></subject><relatedItem type="host"><titleInfo><title>Chemical Engineering & Processing: Process Intensification</title></titleInfo><titleInfo type="abbreviated"><title>CEP</title></titleInfo><genre type="journal" authority="ISTEX" authorityURI="https://publication-type.data.istex.fr" valueURI="https://publication-type.data.istex.fr/ark:/67375/JMC-0GLKJH51-B">journal</genre><originInfo><publisher>ELSEVIER</publisher><dateIssued encoding="w3cdtf">200102</dateIssued></originInfo><identifier type="ISSN">0255-2701</identifier><identifier type="PII">S0255-2701(00)X0022-0</identifier><part><date>200102</date><detail type="volume"><number>40</number><caption>vol.</caption></detail><detail type="issue"><number>2</number><caption>no.</caption></detail><extent unit="issue-pages"><start>85</start><end>194</end></extent><extent unit="pages"><start>129</start><end>133</end></extent></part></relatedItem><identifier type="istex">528E6054FC6FECF5356EEC304ADCC8838D9A7CD5</identifier><identifier type="ark">ark:/67375/6H6-C7S0Z7V6-H</identifier><identifier type="DOI">10.1016/S0255-2701(00)00132-X</identifier><identifier type="PII">S0255-2701(00)00132-X</identifier><accessCondition type="use and reproduction" contentType="copyright">©2001 Elsevier Science B.V.</accessCondition><recordInfo><recordContentSource authority="ISTEX" authorityURI="https://loaded-corpus.data.istex.fr" valueURI="https://loaded-corpus.data.istex.fr/ark:/67375/XBH-HKKZVM7B-M">elsevier</recordContentSource><recordOrigin>Elsevier Science B.V., ©2001</recordOrigin></recordInfo></mods><json:item><extension>json</extension><original>false</original><mimetype>application/json</mimetype><uri>https://api.istex.fr/document/528E6054FC6FECF5356EEC304ADCC8838D9A7CD5/metadata/json</uri></json:item></metadata><serie></serie></istex></record>Pour manipuler ce document sous Unix (Dilib)
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