An energetic analysis of CO2 capture on a gas turbine combining flue gas recirculation and membrane separation
Identifieur interne : 000089 ( Hal/Curation ); précédent : 000088; suivant : 000090An energetic analysis of CO2 capture on a gas turbine combining flue gas recirculation and membrane separation
Auteurs : Bouchra Belaissaoui [France] ; Gilles Cabot [France] ; Marie-Sophie Cabot [France] ; David Wilson [États-Unis] ; Eric Favre [France]Source :
- Energy [ 0360-5442 ] ; 2012.
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Abstract
Post-combustion Carbon Capture and Storage (CCS) is currently intensively investigated as a key issue for the mitigation of greenhouse gases emissions. A very large number of studies is dedicated to coal power plants. In this paper, the possibility to achieve carbon capture on a gas turbine, based on a combination of flue gas recycle and membrane separation is reported. Membrane processes are effectively known to offer attractive performances in terms of energy efficiency, as soon as concentrated and/or pressure mixtures have to be treated. Two different flow schemes have been simulated and compared: flue gas recycle with air combustion and flue gas recycle with an oxygen enriched feed mixture. The energy requirement of the different processes, expressed in GJ (thermal basis) per ton of recovered CO2, and the size of the membrane capture process (expressed in m(2) of membrane area) have been systematically estimated for different membrane separation performances. It is shown that an overall energy requirement down to 2.6 GJ per ton can possibly be achieved when optimal operating conditions, based on oxygen enriched air (OEA) combustion together with a highly selective membrane (CO2/N-2 selectivity of 200) are combined. Additional possibilities in order to minimise the energy penalty of the process are discussed.
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DOI: 10.1016/j.energy.2011.12.018
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A very large number of studies is dedicated to coal power plants. In this paper, the possibility to achieve carbon capture on a gas turbine, based on a combination of flue gas recycle and membrane separation is reported. Membrane processes are effectively known to offer attractive performances in terms of energy efficiency, as soon as concentrated and/or pressure mixtures have to be treated. Two different flow schemes have been simulated and compared: flue gas recycle with air combustion and flue gas recycle with an oxygen enriched feed mixture. The energy requirement of the different processes, expressed in GJ (thermal basis) per ton of recovered CO2, and the size of the membrane capture process (expressed in m(2) of membrane area) have been systematically estimated for different membrane separation performances. It is shown that an overall energy requirement down to 2.6 GJ per ton can possibly be achieved when optimal operating conditions, based on oxygen enriched air (OEA) combustion together with a highly selective membrane (CO2/N-2 selectivity of 200) are combined. Additional possibilities in order to minimise the energy penalty of the process are discussed.</div></front></TEI><hal api="V3"><titleStmt><title xml:lang="en">An energetic analysis of CO2 capture on a gas turbine combining flue gas recirculation and membrane separation</title><author role="aut"><persName><forename type="first">Bouchra</forename><surname>Belaissaoui</surname></persName><email></email><idno type="halauthor">475716</idno><affiliation ref="#struct-211875"></affiliation></author><author role="aut"><persName><forename type="first">Gilles</forename><surname>Cabot</surname></persName><email></email><idno type="halauthor">805916</idno><affiliation ref="#struct-962"></affiliation></author><author role="aut"><persName><forename type="first">Marie-Sophie</forename><surname>Cabot</surname></persName><email></email><idno type="halauthor">805917</idno><affiliation ref="#struct-962"></affiliation></author><author role="aut"><persName><forename type="first">David</forename><surname>Wilson</surname></persName><email></email><idno type="halauthor">805899</idno><affiliation ref="#struct-211716"></affiliation></author><author role="crp"><persName><forename type="first">Eric</forename><surname>Favre</surname></persName><email>eric.favre@univ-lorraine.fr</email><idno type="halauthor">805900</idno><affiliation ref="#struct-211875"></affiliation></author><editor role="depositor"><persName><forename>Gabriel</forename><surname>Wild</surname></persName><email>gabriel.wild@univ-lorraine.fr</email></editor><funder>CNRS PIE COCASE</funder></titleStmt><editionStmt><edition n="v1" type="current"><date type="whenSubmitted">2013-01-15 14:59:47</date><date type="whenWritten">2011</date><date type="whenModified">2016-05-11 01:05:30</date><date type="whenReleased">2013-01-15 14:59:47</date><date type="whenProduced">2012</date></edition><respStmt><resp>contributor</resp><name key="179637"><persName><forename>Gabriel</forename><surname>Wild</surname></persName><email>gabriel.wild@univ-lorraine.fr</email></name></respStmt></editionStmt><publicationStmt><distributor>CCSD</distributor><idno type="halId">hal-00776411</idno><idno type="halUri">https://hal.archives-ouvertes.fr/hal-00776411</idno><idno type="halBibtex">belaissaoui:hal-00776411</idno><idno type="halRefHtml">Energy, Elsevier, 2012, 38 (1), pp.167-175. <10.1016/j.energy.2011.12.018></idno><idno type="halRef">Energy, Elsevier, 2012, 38 (1), pp.167-175. <10.1016/j.energy.2011.12.018></idno></publicationStmt><seriesStmt><idno type="stamp" n="CNRS">CNRS - Centre national de la recherche scientifique</idno><idno type="stamp" n="UNIV-ROUEN">Université de Rouen</idno><idno type="stamp" n="CORIA">Complexe de recherche interprofessionnel en aerothermochimie</idno><idno type="stamp" n="LRGP-UL">LRGP</idno><idno type="stamp" n="COMUE-NORMANDIE">Normandie Université</idno><idno type="stamp" n="UNIV-LORRAINE">Université de Lorraine</idno></seriesStmt><notesStmt><note type="audience" n="2">International</note><note type="popular" n="0">No</note><note type="peer" n="1">Yes</note></notesStmt><sourceDesc><biblStruct><analytic><title xml:lang="en">An energetic analysis of CO2 capture on a gas turbine combining flue gas recirculation and membrane separation</title><author role="aut"><persName><forename type="first">Bouchra</forename><surname>Belaissaoui</surname></persName><idno type="halAuthorId">475716</idno><affiliation ref="#struct-211875"></affiliation></author><author role="aut"><persName><forename type="first">Gilles</forename><surname>Cabot</surname></persName><idno type="halAuthorId">805916</idno><affiliation ref="#struct-962"></affiliation></author><author role="aut"><persName><forename type="first">Marie-Sophie</forename><surname>Cabot</surname></persName><idno type="halAuthorId">805917</idno><affiliation ref="#struct-962"></affiliation></author><author role="aut"><persName><forename type="first">David</forename><surname>Wilson</surname></persName><idno type="halAuthorId">805899</idno><affiliation ref="#struct-211716"></affiliation></author><author role="crp"><persName><forename type="first">Eric</forename><surname>Favre</surname></persName><email>eric.favre@univ-lorraine.fr</email><idno type="halAuthorId">805900</idno><affiliation ref="#struct-211875"></affiliation></author></analytic><monogr><idno type="halJournalId" status="VALID">4620</idno><idno type="issn">0360-5442</idno><idno type="eissn">0360-5442</idno><title level="j">Energy</title><imprint><publisher>Elsevier</publisher><biblScope unit="volume">38</biblScope><biblScope unit="issue">1</biblScope><biblScope unit="pp">167-175</biblScope><date type="datePub">2012</date></imprint></monogr><idno type="doi">10.1016/j.energy.2011.12.018</idno></biblStruct></sourceDesc><profileDesc><langUsage><language ident="en">English</language></langUsage><textClass><keywords scheme="author"><term xml:lang="en">CO2</term><term xml:lang="en">Capture</term><term xml:lang="en">Gas turbine</term><term xml:lang="en">Membranes</term><term xml:lang="en">Flue gas</term><term xml:lang="en">CARBON-DIOXIDE CAPTURE</term><term xml:lang="en">FACILITATED TRANSPORT MEMBRANE</term><term xml:lang="en">POSTCOMBUSTION CAPTURE</term><term xml:lang="en">POWER-PLANT</term><term xml:lang="en">BLEND MEMBRANE</term><term xml:lang="en">COMBUSTION</term><term xml:lang="en">AIR</term><term xml:lang="en">PERFORMANCE</term><term xml:lang="en">TECHNOLOGY</term><term xml:lang="en">ABSORPTION</term></keywords><classCode scheme="halDomain" n="spi.gproc">Engineering Sciences [physics]/Chemical and Process Engineering</classCode><classCode scheme="halTypology" n="ART">Journal articles</classCode></textClass><abstract xml:lang="en">Post-combustion Carbon Capture and Storage (CCS) is currently intensively investigated as a key issue for the mitigation of greenhouse gases emissions. A very large number of studies is dedicated to coal power plants. In this paper, the possibility to achieve carbon capture on a gas turbine, based on a combination of flue gas recycle and membrane separation is reported. Membrane processes are effectively known to offer attractive performances in terms of energy efficiency, as soon as concentrated and/or pressure mixtures have to be treated. Two different flow schemes have been simulated and compared: flue gas recycle with air combustion and flue gas recycle with an oxygen enriched feed mixture. The energy requirement of the different processes, expressed in GJ (thermal basis) per ton of recovered CO2, and the size of the membrane capture process (expressed in m(2) of membrane area) have been systematically estimated for different membrane separation performances. It is shown that an overall energy requirement down to 2.6 GJ per ton can possibly be achieved when optimal operating conditions, based on oxygen enriched air (OEA) combustion together with a highly selective membrane (CO2/N-2 selectivity of 200) are combined. Additional possibilities in order to minimise the energy penalty of the process are discussed.</abstract></profileDesc></hal></record>Pour manipuler ce document sous Unix (Dilib)
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