Secagem de pêra em secador a microondas

Detalhes bibliográficos
Autor(a) principal: Fumagalli, Fabíola
Data de Publicação: 2003
Tipo de documento: Dissertação
Idioma: por
Título da fonte: Repositório Institucional da UFSCAR
Texto Completo: https://repositorio.ufscar.br/handle/ufscar/4056
Resumo: The present work has as main objective the pear drying in three different dryers: convective, microwave and microwave-convective. It is also intended to evaluate the effect of the osmotic dehydration, as pré-treatment, in the quality of the dried product. Before they be dried or dehydrated the samples passed by a mechanical treatment, which consists of peeling, seeds removing and cutting the fruit, and a chemical treatment with its immersion in solution 1,5% of ascorbic acid for 15 minutes. The stage of osmotic dehydration was carried out by analying the influence of the osmotic agent concentration (sucrose to 25; 37,5 and 50%), of the temperature (30, 40 and 50ºC), of the sample geometry (cubes, toothpicks and slices) and of the use of agitation (0 and 120 rpm) in the kinetics of the process, through the loss of water and the sucrose incorporation by the fruit. The best kinetic condition obtained, through statistical analysis of the data, was to the sample in slices dehydrated at 40ºC, with 37,5% of sucrose and without agitation, being this condition used as pretreatment to the drying. The adjustment of the experimental data was accomplished by the empirical model of Azuara (1992). The drying stage was studied for the fresh and osmotically dehydrated fruit. In this stage, the best kinetic condition was stablished based on the analysis of the influence of the kind of drying used and the power of the microwave in the moisture content of the fruit. The speed and temperature of the air was maintained constant at 2 m/s and 50ºC, and the temperature inside the sample was measured during drying. The best kinetic condition obtained was for the microwave-convective drying at 0,3W/g of osmotically dehydrated samples. The adjustment of the experimental data was accomplished by the Lewis (1921) and Page difusion models (1949). The materials and products of the osmotic dehydration and drying were analyzed concerning their quality, being the main analyses, calcium, phosphorus, potassium, water activity, density, moisture content, total solids and shrink. The results obtained were compared in terms of the drying kinetics and quality of the product, for the equipments used through statistical treatment and with available data from the literature. The osmotic dehydration had beneficial effects on the properties analyzed, giving the best results to the main components detention and maintenance of the others analyzed properties. During the drying, the quality decreases with the increase in the inner sample temperature. The shrink data adjustment, presented by the volume decrease, was well represented by the Lozano et al. (1983) model, being linearly proportional to the moisture content variation.
id SCAR_880c07d3990177324b169ad6a65b230b
oai_identifier_str oai:repositorio.ufscar.br:ufscar/4056
network_acronym_str SCAR
network_name_str Repositório Institucional da UFSCAR
repository_id_str 4322
spelling Fumagalli, FabíolaSilveira, Ana Maria dahttp://genos.cnpq.br:12010/dwlattes/owa/prc_imp_cv_int?f_cod=K4787572Z9http://genos.cnpq.br:12010/dwlattes/owa/prc_imp_cv_int?f_cod=K4762775P2013cf7df-ea32-4288-959e-f2559b4467fa2016-06-02T19:56:41Z2005-01-072016-06-02T19:56:41Z2003-08-05FUMAGALLI, Fabíola. Secagem de pêra em secador a microondas.. 2003. 147 f. Dissertação (Mestrado em Ciências Exatas e da Terra) - Universidade Federal de São Carlos, São Carlos, 2003.https://repositorio.ufscar.br/handle/ufscar/4056The present work has as main objective the pear drying in three different dryers: convective, microwave and microwave-convective. It is also intended to evaluate the effect of the osmotic dehydration, as pré-treatment, in the quality of the dried product. Before they be dried or dehydrated the samples passed by a mechanical treatment, which consists of peeling, seeds removing and cutting the fruit, and a chemical treatment with its immersion in solution 1,5% of ascorbic acid for 15 minutes. The stage of osmotic dehydration was carried out by analying the influence of the osmotic agent concentration (sucrose to 25; 37,5 and 50%), of the temperature (30, 40 and 50ºC), of the sample geometry (cubes, toothpicks and slices) and of the use of agitation (0 and 120 rpm) in the kinetics of the process, through the loss of water and the sucrose incorporation by the fruit. The best kinetic condition obtained, through statistical analysis of the data, was to the sample in slices dehydrated at 40ºC, with 37,5% of sucrose and without agitation, being this condition used as pretreatment to the drying. The adjustment of the experimental data was accomplished by the empirical model of Azuara (1992). The drying stage was studied for the fresh and osmotically dehydrated fruit. In this stage, the best kinetic condition was stablished based on the analysis of the influence of the kind of drying used and the power of the microwave in the moisture content of the fruit. The speed and temperature of the air was maintained constant at 2 m/s and 50ºC, and the temperature inside the sample was measured during drying. The best kinetic condition obtained was for the microwave-convective drying at 0,3W/g of osmotically dehydrated samples. The adjustment of the experimental data was accomplished by the Lewis (1921) and Page difusion models (1949). The materials and products of the osmotic dehydration and drying were analyzed concerning their quality, being the main analyses, calcium, phosphorus, potassium, water activity, density, moisture content, total solids and shrink. The results obtained were compared in terms of the drying kinetics and quality of the product, for the equipments used through statistical treatment and with available data from the literature. The osmotic dehydration had beneficial effects on the properties analyzed, giving the best results to the main components detention and maintenance of the others analyzed properties. During the drying, the quality decreases with the increase in the inner sample temperature. The shrink data adjustment, presented by the volume decrease, was well represented by the Lozano et al. (1983) model, being linearly proportional to the moisture content variation.O presente trabalho teve como objetivo principal a secagem de pêra em três diferentes secadores: convectivo, microondas e combinado microondas-convectivo. Pretende-se também avaliar o efeito da desidratação osmótica, como pré-tratamento, na qualidade do produto seco. Antes de serem secas ou desidratadas as amostras passaram por um tratamento mecânico, que consistiu em descascar, retirar sementes e cortar a fruta, e por um tratamento químico com sua imersão em solução 1,5% de ácido ascórbico durante 15 minutos. A etapa de desidratação osmótica foi conduzida analisando-se a influência da concentração do agente osmótico (sacarose a 25; 37,5 e 50%), da temperatura (30, 40 e 50ºC), da geometria da amostra (cubos, palitos e fatias) e do uso ou não de agitação (0 e 120 rpm) na cinética do processo, através da perda de água e da incorporação de sacarose pela fruta. A melhor condição cinética obtida, através de análise estatística dos dados, foi para a amostra em fatias desidratada a 40ºC, com 37,5% de sacarose e sem agitação, sendo esta condição utilizada como pré-tratamento à secagem. O ajuste dos dados experimentais foi realizado pelo modelo empírico de Azuara et al. (1992). A etapa de secagem foi estudada para a fruta in natura e desidratada osmoticamente. Nesta etapa, a melhor condição cinética foi determinada pela análise da influência do tipo de secagem e da potência de microondas no teor de umidade final da fruta. A velocidade e a temperatura do ar foram mantidas constantes em 2m/s e 50ºC, respectivamente e mediu-se a temperatura no interior da amostra durante a secagem. A melhor condição cinética obtida foi para a secagem no modo combinado microondas-convectivo com potência de 0,3 W/(g amostra) para amostras pré-desidratadas osmoticamente. O ajuste dos dados experimentais foi realizado utilizando-se os modelos de Lewis (1921) e difusional de Page (1949), apresentando bons resultados. Os materiais e produtos da desidratação osmótica e da secagem foram analisados quanto a sua qualidade, sendo as principais análises, cálcio, fósforo, potássio, atividade da água, densidade, teor de umidade, sólidos totais e encolhimento. A desidratação osmótica demonstrou ter efeito benéfico nas características físico-químicas analisadas, contribuindo para a retenção dos principais constituintes e manutenção das demais características analisadas. Na secagem, a qualidade cai com o aumento da temperatura no interior da amostra. O encolhimento, dado pela redução no volume, foi bem representado pelo modelo de Lozano et al. (1983), sendo linearmente proporcional a variação no teor de umidade.Universidade Federal de Sao Carlosapplication/pdfporUniversidade Federal de São CarlosPrograma de Pós-Graduação em Engenharia Química - PPGEQUFSCarBRSecagem e desidrataçãoPêraEncolhimentoDesidratação osmóticaMicroondasENGENHARIAS::ENGENHARIA QUIMICASecagem de pêra em secador a microondasinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/masterThesis-1-1076309f7-a9e4-4cfe-81da-03b94e6ea4aainfo:eu-repo/semantics/openAccessreponame:Repositório Institucional da UFSCARinstname:Universidade Federal de São Carlos (UFSCAR)instacron:UFSCARORIGINALDissFF.pdfapplication/pdf843994https://repositorio.ufscar.br/bitstream/ufscar/4056/1/DissFF.pdffd055fe92de7017d191025abd3b9a1e4MD51THUMBNAILDissFF.pdf.jpgDissFF.pdf.jpgIM Thumbnailimage/jpeg8658https://repositorio.ufscar.br/bitstream/ufscar/4056/2/DissFF.pdf.jpgc5c447d92828909a508e0b9426479115MD52ufscar/40562023-09-18 18:31:46.021oai:repositorio.ufscar.br:ufscar/4056Repositório InstitucionalPUBhttps://repositorio.ufscar.br/oai/requestopendoar:43222023-09-18T18:31:46Repositório Institucional da UFSCAR - Universidade Federal de São Carlos (UFSCAR)false
dc.title.por.fl_str_mv Secagem de pêra em secador a microondas
title Secagem de pêra em secador a microondas
spellingShingle Secagem de pêra em secador a microondas
Fumagalli, Fabíola
Secagem e desidratação
Pêra
Encolhimento
Desidratação osmótica
Microondas
ENGENHARIAS::ENGENHARIA QUIMICA
title_short Secagem de pêra em secador a microondas
title_full Secagem de pêra em secador a microondas
title_fullStr Secagem de pêra em secador a microondas
title_full_unstemmed Secagem de pêra em secador a microondas
title_sort Secagem de pêra em secador a microondas
author Fumagalli, Fabíola
author_facet Fumagalli, Fabíola
author_role author
dc.contributor.authorlattes.por.fl_str_mv http://genos.cnpq.br:12010/dwlattes/owa/prc_imp_cv_int?f_cod=K4762775P2
dc.contributor.author.fl_str_mv Fumagalli, Fabíola
dc.contributor.advisor1.fl_str_mv Silveira, Ana Maria da
dc.contributor.advisor1Lattes.fl_str_mv http://genos.cnpq.br:12010/dwlattes/owa/prc_imp_cv_int?f_cod=K4787572Z9
dc.contributor.authorID.fl_str_mv 013cf7df-ea32-4288-959e-f2559b4467fa
contributor_str_mv Silveira, Ana Maria da
dc.subject.por.fl_str_mv Secagem e desidratação
Pêra
Encolhimento
Desidratação osmótica
Microondas
topic Secagem e desidratação
Pêra
Encolhimento
Desidratação osmótica
Microondas
ENGENHARIAS::ENGENHARIA QUIMICA
dc.subject.cnpq.fl_str_mv ENGENHARIAS::ENGENHARIA QUIMICA
description The present work has as main objective the pear drying in three different dryers: convective, microwave and microwave-convective. It is also intended to evaluate the effect of the osmotic dehydration, as pré-treatment, in the quality of the dried product. Before they be dried or dehydrated the samples passed by a mechanical treatment, which consists of peeling, seeds removing and cutting the fruit, and a chemical treatment with its immersion in solution 1,5% of ascorbic acid for 15 minutes. The stage of osmotic dehydration was carried out by analying the influence of the osmotic agent concentration (sucrose to 25; 37,5 and 50%), of the temperature (30, 40 and 50ºC), of the sample geometry (cubes, toothpicks and slices) and of the use of agitation (0 and 120 rpm) in the kinetics of the process, through the loss of water and the sucrose incorporation by the fruit. The best kinetic condition obtained, through statistical analysis of the data, was to the sample in slices dehydrated at 40ºC, with 37,5% of sucrose and without agitation, being this condition used as pretreatment to the drying. The adjustment of the experimental data was accomplished by the empirical model of Azuara (1992). The drying stage was studied for the fresh and osmotically dehydrated fruit. In this stage, the best kinetic condition was stablished based on the analysis of the influence of the kind of drying used and the power of the microwave in the moisture content of the fruit. The speed and temperature of the air was maintained constant at 2 m/s and 50ºC, and the temperature inside the sample was measured during drying. The best kinetic condition obtained was for the microwave-convective drying at 0,3W/g of osmotically dehydrated samples. The adjustment of the experimental data was accomplished by the Lewis (1921) and Page difusion models (1949). The materials and products of the osmotic dehydration and drying were analyzed concerning their quality, being the main analyses, calcium, phosphorus, potassium, water activity, density, moisture content, total solids and shrink. The results obtained were compared in terms of the drying kinetics and quality of the product, for the equipments used through statistical treatment and with available data from the literature. The osmotic dehydration had beneficial effects on the properties analyzed, giving the best results to the main components detention and maintenance of the others analyzed properties. During the drying, the quality decreases with the increase in the inner sample temperature. The shrink data adjustment, presented by the volume decrease, was well represented by the Lozano et al. (1983) model, being linearly proportional to the moisture content variation.
publishDate 2003
dc.date.issued.fl_str_mv 2003-08-05
dc.date.available.fl_str_mv 2005-01-07
2016-06-02T19:56:41Z
dc.date.accessioned.fl_str_mv 2016-06-02T19:56:41Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/masterThesis
format masterThesis
status_str publishedVersion
dc.identifier.citation.fl_str_mv FUMAGALLI, Fabíola. Secagem de pêra em secador a microondas.. 2003. 147 f. Dissertação (Mestrado em Ciências Exatas e da Terra) - Universidade Federal de São Carlos, São Carlos, 2003.
dc.identifier.uri.fl_str_mv https://repositorio.ufscar.br/handle/ufscar/4056
identifier_str_mv FUMAGALLI, Fabíola. Secagem de pêra em secador a microondas.. 2003. 147 f. Dissertação (Mestrado em Ciências Exatas e da Terra) - Universidade Federal de São Carlos, São Carlos, 2003.
url https://repositorio.ufscar.br/handle/ufscar/4056
dc.language.iso.fl_str_mv por
language por
dc.relation.confidence.fl_str_mv -1
-1
dc.relation.authority.fl_str_mv 076309f7-a9e4-4cfe-81da-03b94e6ea4aa
dc.rights.driver.fl_str_mv info:eu-repo/semantics/openAccess
eu_rights_str_mv openAccess
dc.format.none.fl_str_mv application/pdf
dc.publisher.none.fl_str_mv Universidade Federal de São Carlos
dc.publisher.program.fl_str_mv Programa de Pós-Graduação em Engenharia Química - PPGEQ
dc.publisher.initials.fl_str_mv UFSCar
dc.publisher.country.fl_str_mv BR
publisher.none.fl_str_mv Universidade Federal de São Carlos
dc.source.none.fl_str_mv reponame:Repositório Institucional da UFSCAR
instname:Universidade Federal de São Carlos (UFSCAR)
instacron:UFSCAR
instname_str Universidade Federal de São Carlos (UFSCAR)
instacron_str UFSCAR
institution UFSCAR
reponame_str Repositório Institucional da UFSCAR
collection Repositório Institucional da UFSCAR
bitstream.url.fl_str_mv https://repositorio.ufscar.br/bitstream/ufscar/4056/1/DissFF.pdf
https://repositorio.ufscar.br/bitstream/ufscar/4056/2/DissFF.pdf.jpg
bitstream.checksum.fl_str_mv fd055fe92de7017d191025abd3b9a1e4
c5c447d92828909a508e0b9426479115
bitstream.checksumAlgorithm.fl_str_mv MD5
MD5
repository.name.fl_str_mv Repositório Institucional da UFSCAR - Universidade Federal de São Carlos (UFSCAR)
repository.mail.fl_str_mv
_version_ 1813715532731383808