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dc.contributor.authorSaucedo, Marco Aen
dc.contributor.authorDennis, Johnen
dc.contributor.authorScott, Stuart Aen
dc.date.accessioned2014-07-15T14:06:20Z
dc.date.available2014-07-15T14:06:20Z
dc.date.issued2014-07-15en
dc.identifier.citationProceedings of the Combustion Institute Volume 35, Issue 3, 2015, Pages 2785–2792. DOI: 10.1016/j.proci.2014.07.005
dc.identifier.issn1540-7489
dc.identifier.urihttps://www.repository.cam.ac.uk/handle/1810/245512
dc.description.abstractRates of gasification of lignite char were compared when gasification with CO2 was undertaken in a fluidised bed of either (i) an active Fe-based oxygen carrier used for chemical looping or (ii) inert sand. The kinetics of the gasification were found to be significantly faster in the presence of the oxygen carrier, especially at temperatures above 1123 K. An analytical solution assuming pseudo-binary diffusion of species was developed to account for external and internal mass transfer and for the effect of the looping agent. The model also included the effects of the evolution of the pore structure at different conversions. The results are compared with a full numerical model using the Stefan-Maxwell equations. Excellent agreement was observed between the rates predicted by the two models and those observed experimentally at T ≤ 1123 K. At 1173 K, the pseudo-binary model predicted slightly higher rates than the full numerical solution. It was found that a significant share of the error of the predicted rates with the analytical solution was caused by an underestimation of intraparticle diffusional resistance rather than by assuming a pseudo-binary system external to the particle. Both models suggested that the presence of Fe2O3 led to an increase in the rate of gasification because of the rapid oxidation of CO by the oxygen carrier to CO2. This resulted in the removal of CO and maintained a higher mole fraction of CO2 in the mixture of gas around the particle of char, i.e. within the mass transfer boundary layer surrounding the particle. This effect was most prominent at ~20% conversion when (i) the surface area for reaction was a maximum and (ii) because of the accompanying increase in porosity, intraparticle resistance to gas mass transfer within the particle of char had fallen, compared with that in the initial particle.
dc.description.sponsorshipEPSRC
dc.languageEnglishen
dc.language.isoenen
dc.rightsDSpace@Cambridge license
dc.subjectChemical-looping combustionen
dc.subjectgasificationen
dc.subjectcoalen
dc.subjectCO2 separationen
dc.subjectfluidisationen
dc.titleModelling Rates of Gasification of a Char Particle in Chemical Looping Combustionen
dc.typeArticle
dc.description.versionThis is the author accepted manuscript. The final version is now available at http://www.sciencedirect.com/science/article/pii/S1540748914003150.en
prism.endingPage2792
prism.publicationDate2014en
prism.publicationNameProceedings of the Combustion Instituteen
prism.startingPage2785
prism.volume35en
dc.rioxxterms.funderEPSRC
rioxxterms.versionofrecord10.1016/j.proci.2014.07.005en
rioxxterms.licenseref.urihttp://www.rioxx.net/licenses/all-rights-reserveden
rioxxterms.licenseref.startdate2014-07-15en
dc.contributor.orcidDennis, John [0000-0002-5014-5676]
dc.identifier.eissn1873-2704
rioxxterms.typeJournal Article/Reviewen
pubs.funder-project-idEPSRC (EP/G063265/1)
rioxxterms.freetoread.startdate2015-07-30


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