Convective drying kinetics of osmotically pretreated papaya cubes

Detalhes bibliográficos
Autor(a) principal: Ferreira,João P. de L.
Data de Publicação: 2020
Outros Autores: Castro,Deise S. de, Moreira,Inacia dos S., Silva,Wilton P. da, Figueirêdo,Rossana M. F. de, Queiroz,Alexandre J. de M.
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=S1415-43662020000300200
Resumo: ABSTRACT This study assessed the fitting of mathematical models to the convective drying kinetics of osmotically pre-dehydrated papaya cubes. Papaya cubes were subjected to osmotic dehydration in sucrose solutions at 40 and 50 ºBrix, at temperatures of 50 and 60 ºC, followed by complementary convective drying in forced air circulation oven under three temperatures (50, 60 and 70 °C) and constant air velocity of 1.0 m s-1. Ten thin-layer drying mathematical models were fitted to the experimental data. The increase in air temperature and the decrease in osmotic solution concentration resulted in increased water removal rate. Based on the statistical indices, the Two Terms model was the one that best described the drying kinetics of the samples for all evaluated conditions. The effective diffusion coefficients increased with the elevation of air temperature, ranging from 1.766 x 10-10 to 3.910 x 10-6 m2 s-1, whereas the convective mass transfer coefficients ranged from 3.910 x 10-7 to 1.201 x 10-6 m s-1 with Biot number from 0.001 to 12.500.
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spelling Convective drying kinetics of osmotically pretreated papaya cubesCarica papayaosmotic dehydrationeffective diffusivityABSTRACT This study assessed the fitting of mathematical models to the convective drying kinetics of osmotically pre-dehydrated papaya cubes. Papaya cubes were subjected to osmotic dehydration in sucrose solutions at 40 and 50 ºBrix, at temperatures of 50 and 60 ºC, followed by complementary convective drying in forced air circulation oven under three temperatures (50, 60 and 70 °C) and constant air velocity of 1.0 m s-1. Ten thin-layer drying mathematical models were fitted to the experimental data. The increase in air temperature and the decrease in osmotic solution concentration resulted in increased water removal rate. Based on the statistical indices, the Two Terms model was the one that best described the drying kinetics of the samples for all evaluated conditions. The effective diffusion coefficients increased with the elevation of air temperature, ranging from 1.766 x 10-10 to 3.910 x 10-6 m2 s-1, whereas the convective mass transfer coefficients ranged from 3.910 x 10-7 to 1.201 x 10-6 m s-1 with Biot number from 0.001 to 12.500.Departamento de Engenharia Agrícola - UFCG2020-03-01info:eu-repo/semantics/articleinfo:eu-repo/semantics/publishedVersiontext/htmlhttp://old.scielo.br/scielo.php?script=sci_arttext&pid=S1415-43662020000300200Revista Brasileira de Engenharia Agrícola e Ambiental v.24 n.3 2020reponame:Revista Brasileira de Engenharia Agrícola e Ambiental (Online)instname:Universidade Federal de Campina Grande (UFCG)instacron:UFCG10.1590/1807-1929/agriambi.v24n3p200-208info:eu-repo/semantics/openAccessFerreira,João P. de L.Castro,Deise S. deMoreira,Inacia dos S.Silva,Wilton P. daFigueirêdo,Rossana M. F. deQueiroz,Alexandre J. de M.eng2020-02-27T00:00:00Zoai:scielo:S1415-43662020000300200Revistahttp://www.scielo.br/rbeaaPUBhttps://old.scielo.br/oai/scielo-oai.php||agriambi@agriambi.com.br1807-19291415-4366opendoar:2020-02-27T00:00Revista Brasileira de Engenharia Agrícola e Ambiental (Online) - Universidade Federal de Campina Grande (UFCG)false
dc.title.none.fl_str_mv Convective drying kinetics of osmotically pretreated papaya cubes
title Convective drying kinetics of osmotically pretreated papaya cubes
spellingShingle Convective drying kinetics of osmotically pretreated papaya cubes
Ferreira,João P. de L.
Carica papaya
osmotic dehydration
effective diffusivity
title_short Convective drying kinetics of osmotically pretreated papaya cubes
title_full Convective drying kinetics of osmotically pretreated papaya cubes
title_fullStr Convective drying kinetics of osmotically pretreated papaya cubes
title_full_unstemmed Convective drying kinetics of osmotically pretreated papaya cubes
title_sort Convective drying kinetics of osmotically pretreated papaya cubes
author Ferreira,João P. de L.
author_facet Ferreira,João P. de L.
Castro,Deise S. de
Moreira,Inacia dos S.
Silva,Wilton P. da
Figueirêdo,Rossana M. F. de
Queiroz,Alexandre J. de M.
author_role author
author2 Castro,Deise S. de
Moreira,Inacia dos S.
Silva,Wilton P. da
Figueirêdo,Rossana M. F. de
Queiroz,Alexandre J. de M.
author2_role author
author
author
author
author
dc.contributor.author.fl_str_mv Ferreira,João P. de L.
Castro,Deise S. de
Moreira,Inacia dos S.
Silva,Wilton P. da
Figueirêdo,Rossana M. F. de
Queiroz,Alexandre J. de M.
dc.subject.por.fl_str_mv Carica papaya
osmotic dehydration
effective diffusivity
topic Carica papaya
osmotic dehydration
effective diffusivity
description ABSTRACT This study assessed the fitting of mathematical models to the convective drying kinetics of osmotically pre-dehydrated papaya cubes. Papaya cubes were subjected to osmotic dehydration in sucrose solutions at 40 and 50 ºBrix, at temperatures of 50 and 60 ºC, followed by complementary convective drying in forced air circulation oven under three temperatures (50, 60 and 70 °C) and constant air velocity of 1.0 m s-1. Ten thin-layer drying mathematical models were fitted to the experimental data. The increase in air temperature and the decrease in osmotic solution concentration resulted in increased water removal rate. Based on the statistical indices, the Two Terms model was the one that best described the drying kinetics of the samples for all evaluated conditions. The effective diffusion coefficients increased with the elevation of air temperature, ranging from 1.766 x 10-10 to 3.910 x 10-6 m2 s-1, whereas the convective mass transfer coefficients ranged from 3.910 x 10-7 to 1.201 x 10-6 m s-1 with Biot number from 0.001 to 12.500.
publishDate 2020
dc.date.none.fl_str_mv 2020-03-01
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dc.language.iso.fl_str_mv eng
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dc.relation.none.fl_str_mv 10.1590/1807-1929/agriambi.v24n3p200-208
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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.24 n.3 2020
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