Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiation
Autor(a) principal: | |
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Data de Publicação: | 2015 |
Outros Autores: | , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Revista Brasileira de Engenharia Agrícola e Ambiental (Online) |
Texto Completo: | http://old.scielo.br/scielo.php?script=sci_arttext&pid=S1415-43662015001201178 |
Resumo: | ABSTRACT Mathematical modeling enables dimensioning of dryers, optimization of drying conditions and the evaluation of process performance. The aim of this research was to describe the behavior of orange bagasse drying using Page's and Fick's second law models, and to assess activation energy (using Arrhenius equation), moisture content, water activity and bulk density of product at the end of the process. The drying experimental assays were performed in 2011 with convective air temperature between 36 and 64 ºC and infrared radiation application time in the range from 23 to 277 s in accordance with the experimental central composite rotatable design. Analysis of variance and F-test were applied to results. At the end of the drying process, moisture content was about 0.09 to 0.87 db and water activity was between 0.25 and 0.87. Bulk density did not vary under studied conditions. Empirical Page's model demonstrated better representation of experimental data than the Fick's model for spheres. Activation energy values were about 18.491; 14.975 and 11.421 kJ mol-1 for infrared application times of 60; 150 e 244 s, respectively. |
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Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiationeffective diffusivitywater activityFick’s modelPage’s modelactivation energyABSTRACT Mathematical modeling enables dimensioning of dryers, optimization of drying conditions and the evaluation of process performance. The aim of this research was to describe the behavior of orange bagasse drying using Page's and Fick's second law models, and to assess activation energy (using Arrhenius equation), moisture content, water activity and bulk density of product at the end of the process. The drying experimental assays were performed in 2011 with convective air temperature between 36 and 64 ºC and infrared radiation application time in the range from 23 to 277 s in accordance with the experimental central composite rotatable design. Analysis of variance and F-test were applied to results. At the end of the drying process, moisture content was about 0.09 to 0.87 db and water activity was between 0.25 and 0.87. Bulk density did not vary under studied conditions. Empirical Page's model demonstrated better representation of experimental data than the Fick's model for spheres. Activation energy values were about 18.491; 14.975 and 11.421 kJ mol-1 for infrared application times of 60; 150 e 244 s, respectively.Departamento de Engenharia Agrícola - UFCG2015-12-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S1415-43662015001201178Revista Brasileira de Engenharia Agrícola e Ambiental v.19 n.12 2015reponame:Revista Brasileira de Engenharia Agrícola e Ambiental (Online)instname:Universidade Federal de Campina Grande (UFCG)instacron:UFCG10.1590/1807-1929/agriambi.v19n12p1178-1184info:eu-repo/semantics/openAccessSánchez-Sáenz,Carolina M.Nascimento,Vânia R. G.Biagi,João D.Oliveira,Rafael A. deeng2015-11-19T00:00:00Zoai:scielo:S1415-43662015001201178Revistahttp://www.scielo.br/rbeaaPUBhttps://old.scielo.br/oai/scielo-oai.php||agriambi@agriambi.com.br1807-19291415-4366opendoar:2015-11-19T00:00Revista Brasileira de Engenharia Agrícola e Ambiental (Online) - Universidade Federal de Campina Grande (UFCG)false |
dc.title.none.fl_str_mv |
Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiation |
title |
Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiation |
spellingShingle |
Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiation Sánchez-Sáenz,Carolina M. effective diffusivity water activity Fick’s model Page’s model activation energy |
title_short |
Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiation |
title_full |
Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiation |
title_fullStr |
Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiation |
title_full_unstemmed |
Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiation |
title_sort |
Mathematical modeling of the drying of orange bagasse associating the convective method and infrared radiation |
author |
Sánchez-Sáenz,Carolina M. |
author_facet |
Sánchez-Sáenz,Carolina M. Nascimento,Vânia R. G. Biagi,João D. Oliveira,Rafael A. de |
author_role |
author |
author2 |
Nascimento,Vânia R. G. Biagi,João D. Oliveira,Rafael A. de |
author2_role |
author author author |
dc.contributor.author.fl_str_mv |
Sánchez-Sáenz,Carolina M. Nascimento,Vânia R. G. Biagi,João D. Oliveira,Rafael A. de |
dc.subject.por.fl_str_mv |
effective diffusivity water activity Fick’s model Page’s model activation energy |
topic |
effective diffusivity water activity Fick’s model Page’s model activation energy |
description |
ABSTRACT Mathematical modeling enables dimensioning of dryers, optimization of drying conditions and the evaluation of process performance. The aim of this research was to describe the behavior of orange bagasse drying using Page's and Fick's second law models, and to assess activation energy (using Arrhenius equation), moisture content, water activity and bulk density of product at the end of the process. The drying experimental assays were performed in 2011 with convective air temperature between 36 and 64 ºC and infrared radiation application time in the range from 23 to 277 s in accordance with the experimental central composite rotatable design. Analysis of variance and F-test were applied to results. At the end of the drying process, moisture content was about 0.09 to 0.87 db and water activity was between 0.25 and 0.87. Bulk density did not vary under studied conditions. Empirical Page's model demonstrated better representation of experimental data than the Fick's model for spheres. Activation energy values were about 18.491; 14.975 and 11.421 kJ mol-1 for infrared application times of 60; 150 e 244 s, respectively. |
publishDate |
2015 |
dc.date.none.fl_str_mv |
2015-12-01 |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S1415-43662015001201178 |
url |
http://old.scielo.br/scielo.php?script=sci_arttext&pid=S1415-43662015001201178 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
10.1590/1807-1929/agriambi.v19n12p1178-1184 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
text/html |
dc.publisher.none.fl_str_mv |
Departamento de Engenharia Agrícola - UFCG |
publisher.none.fl_str_mv |
Departamento de Engenharia Agrícola - UFCG |
dc.source.none.fl_str_mv |
Revista Brasileira de Engenharia Agrícola e Ambiental v.19 n.12 2015 reponame:Revista Brasileira de Engenharia Agrícola e Ambiental (Online) instname:Universidade Federal de Campina Grande (UFCG) instacron:UFCG |
instname_str |
Universidade Federal de Campina Grande (UFCG) |
instacron_str |
UFCG |
institution |
UFCG |
reponame_str |
Revista Brasileira de Engenharia Agrícola e Ambiental (Online) |
collection |
Revista Brasileira de Engenharia Agrícola e Ambiental (Online) |
repository.name.fl_str_mv |
Revista Brasileira de Engenharia Agrícola e Ambiental (Online) - Universidade Federal de Campina Grande (UFCG) |
repository.mail.fl_str_mv |
||agriambi@agriambi.com.br |
_version_ |
1750297684159234048 |