Determination of the kinetic parameters of oxy-fuel combustion of coal with a high ash content
Autor(a) principal: | |
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Data de Publicação: | 2015 |
Outros Autores: | |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Repositório Institucional da UFRGS |
Texto Completo: | http://hdl.handle.net/10183/183058 |
Resumo: | The aim of this study was to determine the kinetic parameters of the oxy-fuel combustion of char from a Brazilian bituminous coal with a high ash content. The char, with a particle diameter of 715 μm, was prepared in a N2 atmosphere at 1173 K. The oxy-fuel combustion assays were performed using a thermobalance at different temperatures and O2/CO2 gas mixtures of different concentrations. According to the unreacted core model, the process is determined by chemical reaction at low temperatures, with an activation energy of 56.7 kJ.kmol-1, a reaction order of 0.5 at 973 K and a reaction order of 0.7 overall. The use of the continuous reaction model did not provide a good fit for the experimental data because the consumption of the particles during the reaction was not constant, as predicted by the model. According to the Langmuir-Hinshelwood model, the activation energy for the first step was 37.3 kJ.kmol-1. |
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Nunes, Keila Guerra PachecoMarcilio, Nilson Romeu2018-10-03T02:36:48Z20150104-6632http://hdl.handle.net/10183/183058001078128The aim of this study was to determine the kinetic parameters of the oxy-fuel combustion of char from a Brazilian bituminous coal with a high ash content. The char, with a particle diameter of 715 μm, was prepared in a N2 atmosphere at 1173 K. The oxy-fuel combustion assays were performed using a thermobalance at different temperatures and O2/CO2 gas mixtures of different concentrations. According to the unreacted core model, the process is determined by chemical reaction at low temperatures, with an activation energy of 56.7 kJ.kmol-1, a reaction order of 0.5 at 973 K and a reaction order of 0.7 overall. The use of the continuous reaction model did not provide a good fit for the experimental data because the consumption of the particles during the reaction was not constant, as predicted by the model. According to the Langmuir-Hinshelwood model, the activation energy for the first step was 37.3 kJ.kmol-1.application/pdfengBrazilian journal of chemical engineering. São Paulo. Vol. 32, no. 1 (Jan./Mar. 2015), p. 211-233EngenhariaCharOxy-fuel combustionThermobalanceKineticDetermination of the kinetic parameters of oxy-fuel combustion of coal with a high ash contentinfo:eu-repo/semantics/articleinfo:eu-repo/semantics/otherinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/openAccessreponame:Repositório Institucional da UFRGSinstname:Universidade Federal do Rio Grande do Sul (UFRGS)instacron:UFRGSORIGINAL001078128.pdfTexto completo (inglês)application/pdf1405355http://www.lume.ufrgs.br/bitstream/10183/183058/1/001078128.pdf8a2395b2a44bd85e3b9cc5e5eefe2b25MD51TEXT001078128.pdf.txt001078128.pdf.txtExtracted Texttext/plain35430http://www.lume.ufrgs.br/bitstream/10183/183058/2/001078128.pdf.txtd457ef642d0b5413347b464e0fcc7b46MD52THUMBNAIL001078128.pdf.jpg001078128.pdf.jpgGenerated Thumbnailimage/jpeg2000http://www.lume.ufrgs.br/bitstream/10183/183058/3/001078128.pdf.jpg145045549c67690f709cc605515c7cf8MD5310183/1830582018-10-25 02:44:32.984246oai:www.lume.ufrgs.br:10183/183058Repositório InstitucionalPUBhttps://lume.ufrgs.br/oai/requestlume@ufrgs.bropendoar:2018-10-25T05:44:32Repositório Institucional da UFRGS - Universidade Federal do Rio Grande do Sul (UFRGS)false |
dc.title.pt_BR.fl_str_mv |
Determination of the kinetic parameters of oxy-fuel combustion of coal with a high ash content |
title |
Determination of the kinetic parameters of oxy-fuel combustion of coal with a high ash content |
spellingShingle |
Determination of the kinetic parameters of oxy-fuel combustion of coal with a high ash content Nunes, Keila Guerra Pacheco Engenharia Char Oxy-fuel combustion Thermobalance Kinetic |
title_short |
Determination of the kinetic parameters of oxy-fuel combustion of coal with a high ash content |
title_full |
Determination of the kinetic parameters of oxy-fuel combustion of coal with a high ash content |
title_fullStr |
Determination of the kinetic parameters of oxy-fuel combustion of coal with a high ash content |
title_full_unstemmed |
Determination of the kinetic parameters of oxy-fuel combustion of coal with a high ash content |
title_sort |
Determination of the kinetic parameters of oxy-fuel combustion of coal with a high ash content |
author |
Nunes, Keila Guerra Pacheco |
author_facet |
Nunes, Keila Guerra Pacheco Marcilio, Nilson Romeu |
author_role |
author |
author2 |
Marcilio, Nilson Romeu |
author2_role |
author |
dc.contributor.author.fl_str_mv |
Nunes, Keila Guerra Pacheco Marcilio, Nilson Romeu |
dc.subject.por.fl_str_mv |
Engenharia |
topic |
Engenharia Char Oxy-fuel combustion Thermobalance Kinetic |
dc.subject.eng.fl_str_mv |
Char Oxy-fuel combustion Thermobalance Kinetic |
description |
The aim of this study was to determine the kinetic parameters of the oxy-fuel combustion of char from a Brazilian bituminous coal with a high ash content. The char, with a particle diameter of 715 μm, was prepared in a N2 atmosphere at 1173 K. The oxy-fuel combustion assays were performed using a thermobalance at different temperatures and O2/CO2 gas mixtures of different concentrations. According to the unreacted core model, the process is determined by chemical reaction at low temperatures, with an activation energy of 56.7 kJ.kmol-1, a reaction order of 0.5 at 973 K and a reaction order of 0.7 overall. The use of the continuous reaction model did not provide a good fit for the experimental data because the consumption of the particles during the reaction was not constant, as predicted by the model. According to the Langmuir-Hinshelwood model, the activation energy for the first step was 37.3 kJ.kmol-1. |
publishDate |
2015 |
dc.date.issued.fl_str_mv |
2015 |
dc.date.accessioned.fl_str_mv |
2018-10-03T02:36:48Z |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article info:eu-repo/semantics/other |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://hdl.handle.net/10183/183058 |
dc.identifier.issn.pt_BR.fl_str_mv |
0104-6632 |
dc.identifier.nrb.pt_BR.fl_str_mv |
001078128 |
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0104-6632 001078128 |
url |
http://hdl.handle.net/10183/183058 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.ispartof.pt_BR.fl_str_mv |
Brazilian journal of chemical engineering. São Paulo. Vol. 32, no. 1 (Jan./Mar. 2015), p. 211-233 |
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info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
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application/pdf |
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