Carbon dioxide absorption by monoethanolamine in hollow fiber membrane contactors: A parametric investigation
Identifieur interne : 000464 ( Istex/Corpus ); précédent : 000463; suivant : 000465Carbon dioxide absorption by monoethanolamine in hollow fiber membrane contactors: A parametric investigation
Auteurs : Noureddine Boucif ; Jean Pierre Corriou ; Denis Roizard ; Eric FavreSource :
- AIChE Journal [ 0001-1541 ] ; 2012-09.
English descriptors
- KwdEn :
- Aiche, Aiche journal, Aiche journal september, Aiche september, American institute, Amine, Bers, Boucif, Boundary conditions, Carbon dioxide, Carbon dioxide absorption, Carbon dioxide removal, Chem, Chemical absorption, Chemical reaction, Comsol multiphysics modeling, Concentration gradients, Contact area, Contactor, Contactor exit, Contactor length, Contactor performance, Contactor shell, Contactors, Countercurrent, Dco2, Dense membrane, Dense membrane contactor, Dependent velocity, Diffusivity, Dimensionless, Dimensionless form, Dimensionless groupings, Dioxide, Enhancement, Enhancement factor, Experimental data, Experimental results, Fossil fuels, Free surface model, Hco2, Hco2 kco2, Hydrophobic membrane, Hydrophobic microporous membrane, Kco2, Liquid concentrations, Liquid phase, Liquid solution, Liquid velocity, Lled pores, Lumen, Many researchers, Mass transfer, Mass transfer zone, Mass transport, Membr, Membrane, Membrane barrier, Membrane contactor, Membrane contactors, Membrane material, Membrane module, Membrane modules, Membrane oxygenator, Membrane pores, Membrane wall, Microporous, Microporous membrane, Microporous membrane contactor, Microporous membrane module, Modeling, Module, Nancy universite, Noticeable effect, Numerical simulations, Online issue, Pdms, Pdms membrane, Polymeric membrane domain, Pore, Process equipments, Reaction parameter, Reaction rate, Reactive absorption, Residence time, Retention time, Reynolds number, Rigorous model, Second order reaction rate, September, Shell compartment, Shell domain, Shell side, Shell sides, Shell solute concentration, Shell velocity, Simulation, Solute, Solute concentration, Steady state, Stream waso, Theoretical models, Theoretical studies, Typical amine solutions, Wide range.
- Teeft :
- Aiche, Aiche journal, Aiche journal september, Aiche september, American institute, Amine, Bers, Boucif, Boundary conditions, Carbon dioxide, Carbon dioxide absorption, Carbon dioxide removal, Chem, Chemical absorption, Chemical reaction, Comsol multiphysics modeling, Concentration gradients, Contact area, Contactor, Contactor exit, Contactor length, Contactor performance, Contactor shell, Contactors, Countercurrent, Dco2, Dense membrane, Dense membrane contactor, Dependent velocity, Diffusivity, Dimensionless, Dimensionless form, Dimensionless groupings, Dioxide, Enhancement, Enhancement factor, Experimental data, Experimental results, Fossil fuels, Free surface model, Hco2, Hco2 kco2, Hydrophobic membrane, Hydrophobic microporous membrane, Kco2, Liquid concentrations, Liquid phase, Liquid solution, Liquid velocity, Lled pores, Lumen, Many researchers, Mass transfer, Mass transfer zone, Mass transport, Membr, Membrane, Membrane barrier, Membrane contactor, Membrane contactors, Membrane material, Membrane module, Membrane modules, Membrane oxygenator, Membrane pores, Membrane wall, Microporous, Microporous membrane, Microporous membrane contactor, Microporous membrane module, Modeling, Module, Nancy universite, Noticeable effect, Numerical simulations, Online issue, Pdms, Pdms membrane, Polymeric membrane domain, Pore, Process equipments, Reaction parameter, Reaction rate, Reactive absorption, Residence time, Retention time, Reynolds number, Rigorous model, Second order reaction rate, September, Shell compartment, Shell domain, Shell side, Shell sides, Shell solute concentration, Shell velocity, Simulation, Solute, Solute concentration, Steady state, Stream waso, Theoretical models, Theoretical studies, Typical amine solutions, Wide range.
Abstract
A mathematical and numerical investigations on the gas–liquid absorption of carbon dioxide in monoethanolamine solutions in a hollow fiber membrane contactor device is described. The reactive absorption mechanism was built based on momentum and mass transport conservation laws in all three compartments involved in the process, i.e., the gas phase, the membrane barrier, and the liquid phase. The liquid absorbing solution flows in the fiber bore in which the velocity is assumed to obey a fully developed laminar flow, and the gas mixture circulates counter‐currently to the liquid flow in the shell side where the velocity is characterized by the Navier‐Stokes momentum balance equations. The average outlet gas and liquid concentrations, the reactive absorption flux, and the gas removal efficiencies are parametrically simulated with operational parameters such as gas flow rate, fresh inlet amine concentrations, and fiber geometrical characteristics. The shell velocity was described by other flow hydrodynamics models besides Navier‐Stokes and their simulated results were favorably compared to experimental data. © 2011 American Institute of Chemical Engineers AIChE J, 2012
Url:
DOI: 10.1002/aic.12791
Links to Exploration step
ISTEX:CDACA623488DED5FBF6D19091168C473C42030ECLe document en format XML
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sides</term><term>Shell solute concentration</term><term>Shell velocity</term><term>Simulation</term><term>Solute</term><term>Solute concentration</term><term>Steady state</term><term>Stream waso</term><term>Theoretical models</term><term>Theoretical studies</term><term>Typical amine solutions</term><term>Wide range</term></keywords></textClass></profileDesc></teiHeader><front><div type="abstract" xml:lang="en">A mathematical and numerical investigations on the gas–liquid absorption of carbon dioxide in monoethanolamine solutions in a hollow fiber membrane contactor device is described. 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et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</json:string><json:string>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</json:string></affiliations></json:item><json:item><name>Jean Pierre Corriou</name><affiliations><json:string>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</json:string></affiliations></json:item><json:item><name>Denis Roizard</name><affiliations><json:string>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</json:string></affiliations></json:item><json:item><name>Eric Favre</name><affiliations><json:string>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</json:string></affiliations></json:item></author><subject><json:item><lang><json:string>eng</json:string></lang><value>absorption</value></json:item><json:item><lang><json:string>eng</json:string></lang><value>mathematical modeling</value></json:item><json:item><lang><json:string>eng</json:string></lang><value>membrane separations</value></json:item><json:item><lang><json:string>eng</json:string></lang><value>Navier‐Stokes equations</value></json:item></subject><articleId><json:string>AIC12791</json:string></articleId><language><json:string>eng</json:string></language><originalGenre><json:string>article</json:string></originalGenre><abstract>A mathematical and numerical investigations on the gas–liquid absorption of carbon dioxide in monoethanolamine solutions in a hollow fiber membrane contactor device is described. The reactive absorption mechanism was built based on momentum and mass transport conservation laws in all three compartments involved in the process, i.e., the gas phase, the membrane barrier, and the liquid phase. The liquid absorbing solution flows in the fiber bore in which the velocity is assumed to obey a fully developed laminar flow, and the gas mixture circulates counter‐currently to the liquid flow in the shell side where the velocity is characterized by the Navier‐Stokes momentum balance equations. The average outlet gas and liquid concentrations, the reactive absorption flux, and the gas removal efficiencies are parametrically simulated with operational parameters such as gas flow rate, fresh inlet amine concentrations, and fiber geometrical characteristics. 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role="corresp"><persName><forename type="first">Noureddine</forename><surname>Boucif</surname></persName><email>Noureddine.Boucif@ensic.u‐nancy.fr</email><affiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France<address><country key="FR"></country></address></affiliation><affiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</affiliation></author><author xml:id="author-0001"><persName><forename type="first">Jean Pierre</forename><surname>Corriou</surname></persName><affiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France<address><country key="FR"></country></address></affiliation></author><author xml:id="author-0002"><persName><forename type="first">Denis</forename><surname>Roizard</surname></persName><affiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France<address><country key="FR"></country></address></affiliation></author><author xml:id="author-0003"><persName><forename type="first">Eric</forename><surname>Favre</surname></persName><affiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France<address><country key="FR"></country></address></affiliation></author><idno type="istex">CDACA623488DED5FBF6D19091168C473C42030EC</idno><idno type="ark">ark:/67375/WNG-7SWNQRJH-S</idno><idno type="DOI">10.1002/aic.12791</idno><idno type="unit">AIC12791</idno><idno type="toTypesetVersion">file:AIC.AIC12791.pdf</idno></analytic><monogr><title level="j" type="main">AIChE Journal</title><title level="j" type="alt">AICHE JOURNAL</title><idno type="pISSN">0001-1541</idno><idno type="eISSN">1547-5905</idno><idno type="book-DOI">10.1002/(ISSN)1547-5905</idno><idno type="book-part-DOI">10.1002/aic.v58.9</idno><idno type="product">AIC</idno><imprint><biblScope unit="vol">58</biblScope><biblScope unit="issue">9</biblScope><biblScope unit="page" from="2843">2843</biblScope><biblScope unit="page" to="2855">2855</biblScope><biblScope unit="page-count">13</biblScope><publisher>Wiley Subscription Services, Inc., A Wiley Company</publisher><pubPlace>Hoboken</pubPlace><date type="published" when="2012-09"></date></imprint></monogr></biblStruct></sourceDesc></fileDesc><profileDesc><abstract xml:lang="en" style="main"><head>Abstract</head><p>A mathematical and numerical investigations on the gas–liquid absorption of carbon dioxide in monoethanolamine solutions in a hollow fiber membrane contactor device is described. The reactive absorption mechanism was built based on momentum and mass transport conservation laws in all three compartments involved in the process, i.e., the gas phase, the membrane barrier, and the liquid phase. The liquid absorbing solution flows in the fiber bore in which the velocity is assumed to obey a fully developed laminar flow, and the gas mixture circulates counter‐currently to the liquid flow in the shell side where the velocity is characterized by the Navier‐Stokes momentum balance equations. The average outlet gas and liquid concentrations, the reactive absorption flux, and the gas removal efficiencies are parametrically simulated with operational parameters such as gas flow rate, fresh inlet amine concentrations, and fiber geometrical characteristics. The shell velocity was described by other flow hydrodynamics models besides Navier‐Stokes and their simulated results were favorably compared to experimental data. © 2011 American Institute of Chemical Engineers AIChE J, 2012</p></abstract><textClass><keywords xml:lang="en"><term xml:id="kwd1">absorption</term><term xml:id="kwd2">mathematical modeling</term><term xml:id="kwd3">membrane separations</term><term xml:id="kwd4">Navier‐Stokes equations</term></keywords><keywords rend="articleCategory"><term>Separations: Materials, Devices, and Processes</term></keywords><keywords rend="tocHeading1"><term>Separations: Materials, Devices, and Processes</term></keywords></textClass><langUsage><language 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France</correspondenceTo><objectNameGroup><objectName elementName="appendix">Appendix</objectName></objectNameGroup><linkGroup><link type="toTypesetVersion" href="file:AIC.AIC12791.pdf"></link></linkGroup></publicationMeta><contentMeta><countGroup><count type="figureTotal" number="14"></count><count type="tableTotal" number="3"></count><count type="referenceTotal" number="41"></count><count type="wordTotal" number="10699"></count></countGroup><titleGroup><title type="main" xml:lang="en">Carbon dioxide absorption by monoethanolamine in hollow fiber membrane contactors: A parametric investigation<link href="#fn2"></link></title></titleGroup><creators><creator xml:id="au1" creatorRole="author" affiliationRef="#af1" corresponding="yes"><personName><givenNames>Noureddine</givenNames><familyName>Boucif</familyName></personName><contactDetails><email normalForm="Noureddine.Boucif@ensic.u-nancy.fr">Noureddine.Boucif@ensic.u‐nancy.fr</email></contactDetails></creator><creator xml:id="au2" creatorRole="author" affiliationRef="#af1"><personName><givenNames>Jean Pierre</givenNames><familyName>Corriou</familyName></personName></creator><creator xml:id="au3" creatorRole="author" affiliationRef="#af1"><personName><givenNames>Denis</givenNames><familyName>Roizard</familyName></personName></creator><creator xml:id="au4" creatorRole="author" affiliationRef="#af1"><personName><givenNames>Eric</givenNames><familyName>Favre</familyName></personName></creator></creators><affiliationGroup><affiliation xml:id="af1" countryCode="FR" type="organization"><unparsedAffiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</unparsedAffiliation></affiliation></affiliationGroup><keywordGroup xml:lang="en" type="author"><keyword xml:id="kwd1">absorption</keyword><keyword xml:id="kwd2">mathematical modeling</keyword><keyword xml:id="kwd3">membrane separations</keyword><keyword xml:id="kwd4">Navier‐Stokes equations</keyword></keywordGroup><abstractGroup><abstract type="main" xml:lang="en"><title type="main">Abstract</title><p>A mathematical and numerical investigations on the gas–liquid absorption of carbon dioxide in monoethanolamine solutions in a hollow fiber membrane contactor device is described. The reactive absorption mechanism was built based on momentum and mass transport conservation laws in all three compartments involved in the process, i.e., the gas phase, the membrane barrier, and the liquid phase. The liquid absorbing solution flows in the fiber bore in which the velocity is assumed to obey a fully developed laminar flow, and the gas mixture circulates counter‐currently to the liquid flow in the shell side where the velocity is characterized by the Navier‐Stokes momentum balance equations. The average outlet gas and liquid concentrations, the reactive absorption flux, and the gas removal efficiencies are parametrically simulated with operational parameters such as gas flow rate, fresh inlet amine concentrations, and fiber geometrical characteristics. The shell velocity was described by other flow hydrodynamics models besides Navier‐Stokes and their simulated results were favorably compared to experimental data. © 2011 American Institute of Chemical Engineers AIChE J, 2012</p></abstract></abstractGroup></contentMeta><noteGroup><note xml:id="fn2"><p>Noureddine. B: On leave from the Département de Chimie Industrielle, Faculté des Sciences de l'Ingénieur, Université de Mascara, Mascara 29000, Algeria</p></note></noteGroup></header></component></istex:document></istex:metadataXml><mods version="3.6"><titleInfo lang="en"><title>Carbon dioxide absorption by monoethanolamine in hollow fiber membrane contactors: A parametric investigation</title></titleInfo><titleInfo type="alternative" contentType="CDATA" lang="en"><title>Carbon dioxide absorption by monoethanolamine in hollow fiber membrane contactors: A parametric investigation</title></titleInfo><name type="personal"><namePart type="given">Noureddine</namePart><namePart type="family">Boucif</namePart><affiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</affiliation><affiliation>E-mail: Noureddine.Boucif@ensic.u‐nancy.fr</affiliation><affiliation>Correspondence address: Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</affiliation><role><roleTerm type="text">author</roleTerm></role></name><name type="personal"><namePart type="given">Jean Pierre</namePart><namePart type="family">Corriou</namePart><affiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</affiliation><role><roleTerm type="text">author</roleTerm></role></name><name type="personal"><namePart type="given">Denis</namePart><namePart type="family">Roizard</namePart><affiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</affiliation><role><roleTerm type="text">author</roleTerm></role></name><name type="personal"><namePart type="given">Eric</namePart><namePart type="family">Favre</namePart><affiliation>Laboratoire Réactions et Génie des Procédés LRGP (UPR 3349 CNRS) Nancy Université, BP 20451 ‐ 1, rue Grandville, F‐54001 Nancy Cedex, France</affiliation><role><roleTerm type="text">author</roleTerm></role></name><typeOfResource>text</typeOfResource><genre type="article" displayLabel="article" authority="ISTEX" authorityURI="https://content-type.data.istex.fr" valueURI="https://content-type.data.istex.fr/ark:/67375/XTP-6N5SZHKN-D">article</genre><originInfo><publisher>Wiley Subscription Services, Inc., A Wiley Company</publisher><place><placeTerm type="text">Hoboken</placeTerm></place><dateIssued encoding="w3cdtf">2012-09</dateIssued><dateCaptured encoding="w3cdtf">2010-10-26</dateCaptured><copyrightDate encoding="w3cdtf">2012</copyrightDate></originInfo><language><languageTerm type="code" authority="rfc3066">en</languageTerm><languageTerm type="code" authority="iso639-2b">eng</languageTerm></language><physicalDescription><extent unit="figures">14</extent><extent unit="tables">3</extent><extent unit="references">41</extent><extent unit="words">10699</extent></physicalDescription><abstract lang="en">A mathematical and numerical investigations on the gas–liquid absorption of carbon dioxide in monoethanolamine solutions in a hollow fiber membrane contactor device is described. The reactive absorption mechanism was built based on momentum and mass transport conservation laws in all three compartments involved in the process, i.e., the gas phase, the membrane barrier, and the liquid phase. The liquid absorbing solution flows in the fiber bore in which the velocity is assumed to obey a fully developed laminar flow, and the gas mixture circulates counter‐currently to the liquid flow in the shell side where the velocity is characterized by the Navier‐Stokes momentum balance equations. The average outlet gas and liquid concentrations, the reactive absorption flux, and the gas removal efficiencies are parametrically simulated with operational parameters such as gas flow rate, fresh inlet amine concentrations, and fiber geometrical characteristics. The shell velocity was described by other flow hydrodynamics models besides Navier‐Stokes and their simulated results were favorably compared to experimental data. © 2011 American Institute of Chemical Engineers AIChE J, 2012</abstract><note type="content">*Noureddine. 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