Flow regime assessment in falling film evaporators using residence time distribution functions

Detalhes bibliográficos
Autor(a) principal: Silveira, Arlan Caldas Pereira
Data de Publicação: 2015
Outros Autores: Tanguy, Gaëlle, Perrone, Ítalo Tuler, Jeantet, Romain, Ducept, Fabrice, Carvalho, Antônio Fernandes de, Schuck, Pierre
Tipo de documento: Artigo
Idioma: eng
Título da fonte: LOCUS Repositório Institucional da UFV
Texto Completo: https://doi.org/10.1016/j.jfoodeng.2015.03.016
http://www.locus.ufv.br/handle/123456789/21881
Resumo: A falling film evaporator (FFE) is an industrial device to concentrate solutions. The aim of this study was to identify the flow regime, and characterize and model the residence time distribution (RTD) functions of a FFE. Experimental runs were carried out with skim milk at three different feed mass flow rates. Flow was characterized using experimental Reynolds number (Ref). The RTD function in the FFE was measured in four sections of the vacuum evaporator equipment. These RTD functions were modeled by a combination of perfectly mixed reactor tanks in series. In this study, when the flow regime changed from wavy-laminar to laminar, the mean residence time increased. The flow was analyzed as a main and a minor retarded flow, where two layers of product flowed through the evaporation tubes. The future of this work consists of extending the RTD approach to other products and operating conditions in the evaporator device.
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spelling Silveira, Arlan Caldas PereiraTanguy, GaëllePerrone, Ítalo TulerJeantet, RomainDucept, FabriceCarvalho, Antônio Fernandes deSchuck, Pierre2018-09-19T16:21:29Z2018-09-19T16:21:29Z2015-0902608774https://doi.org/10.1016/j.jfoodeng.2015.03.016http://www.locus.ufv.br/handle/123456789/21881A falling film evaporator (FFE) is an industrial device to concentrate solutions. The aim of this study was to identify the flow regime, and characterize and model the residence time distribution (RTD) functions of a FFE. Experimental runs were carried out with skim milk at three different feed mass flow rates. Flow was characterized using experimental Reynolds number (Ref). The RTD function in the FFE was measured in four sections of the vacuum evaporator equipment. These RTD functions were modeled by a combination of perfectly mixed reactor tanks in series. In this study, when the flow regime changed from wavy-laminar to laminar, the mean residence time increased. The flow was analyzed as a main and a minor retarded flow, where two layers of product flowed through the evaporation tubes. The future of this work consists of extending the RTD approach to other products and operating conditions in the evaporator device.engJournal of Food Engineeringv. 160, p. 65- 76, set. 2015Elsevier Ltd.info:eu-repo/semantics/openAccessFalling film evaporatorsSkim milkResidence time distributionFlow regimeFlow regime assessment in falling film evaporators using residence time distribution functionsinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/articleapplication/pdfreponame:LOCUS Repositório Institucional da UFVinstname:Universidade Federal de Viçosa (UFV)instacron:UFVORIGINALartigo.pdfartigo.pdftexto completoapplication/pdf4530664https://locus.ufv.br//bitstream/123456789/21881/1/artigo.pdfc43fd945c18de37125f718b31369ed75MD51LICENSElicense.txtlicense.txttext/plain; charset=utf-81748https://locus.ufv.br//bitstream/123456789/21881/2/license.txt8a4605be74aa9ea9d79846c1fba20a33MD52THUMBNAILartigo.pdf.jpgartigo.pdf.jpgIM Thumbnailimage/jpeg6522https://locus.ufv.br//bitstream/123456789/21881/3/artigo.pdf.jpg0ac8013c4a347b334462ea1905da1d3dMD53123456789/218812018-09-19 23:00:44.446oai:locus.ufv.br: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Repositório InstitucionalPUBhttps://www.locus.ufv.br/oai/requestfabiojreis@ufv.bropendoar:21452018-09-20T02:00:44LOCUS Repositório Institucional da UFV - Universidade Federal de Viçosa (UFV)false
dc.title.en.fl_str_mv Flow regime assessment in falling film evaporators using residence time distribution functions
title Flow regime assessment in falling film evaporators using residence time distribution functions
spellingShingle Flow regime assessment in falling film evaporators using residence time distribution functions
Silveira, Arlan Caldas Pereira
Falling film evaporators
Skim milk
Residence time distribution
Flow regime
title_short Flow regime assessment in falling film evaporators using residence time distribution functions
title_full Flow regime assessment in falling film evaporators using residence time distribution functions
title_fullStr Flow regime assessment in falling film evaporators using residence time distribution functions
title_full_unstemmed Flow regime assessment in falling film evaporators using residence time distribution functions
title_sort Flow regime assessment in falling film evaporators using residence time distribution functions
author Silveira, Arlan Caldas Pereira
author_facet Silveira, Arlan Caldas Pereira
Tanguy, Gaëlle
Perrone, Ítalo Tuler
Jeantet, Romain
Ducept, Fabrice
Carvalho, Antônio Fernandes de
Schuck, Pierre
author_role author
author2 Tanguy, Gaëlle
Perrone, Ítalo Tuler
Jeantet, Romain
Ducept, Fabrice
Carvalho, Antônio Fernandes de
Schuck, Pierre
author2_role author
author
author
author
author
author
dc.contributor.author.fl_str_mv Silveira, Arlan Caldas Pereira
Tanguy, Gaëlle
Perrone, Ítalo Tuler
Jeantet, Romain
Ducept, Fabrice
Carvalho, Antônio Fernandes de
Schuck, Pierre
dc.subject.pt-BR.fl_str_mv Falling film evaporators
Skim milk
Residence time distribution
Flow regime
topic Falling film evaporators
Skim milk
Residence time distribution
Flow regime
description A falling film evaporator (FFE) is an industrial device to concentrate solutions. The aim of this study was to identify the flow regime, and characterize and model the residence time distribution (RTD) functions of a FFE. Experimental runs were carried out with skim milk at three different feed mass flow rates. Flow was characterized using experimental Reynolds number (Ref). The RTD function in the FFE was measured in four sections of the vacuum evaporator equipment. These RTD functions were modeled by a combination of perfectly mixed reactor tanks in series. In this study, when the flow regime changed from wavy-laminar to laminar, the mean residence time increased. The flow was analyzed as a main and a minor retarded flow, where two layers of product flowed through the evaporation tubes. The future of this work consists of extending the RTD approach to other products and operating conditions in the evaporator device.
publishDate 2015
dc.date.issued.fl_str_mv 2015-09
dc.date.accessioned.fl_str_mv 2018-09-19T16:21:29Z
dc.date.available.fl_str_mv 2018-09-19T16:21:29Z
dc.type.status.fl_str_mv info:eu-repo/semantics/publishedVersion
dc.type.driver.fl_str_mv info:eu-repo/semantics/article
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dc.identifier.uri.fl_str_mv https://doi.org/10.1016/j.jfoodeng.2015.03.016
http://www.locus.ufv.br/handle/123456789/21881
dc.identifier.issn.none.fl_str_mv 02608774
identifier_str_mv 02608774
url https://doi.org/10.1016/j.jfoodeng.2015.03.016
http://www.locus.ufv.br/handle/123456789/21881
dc.language.iso.fl_str_mv eng
language eng
dc.relation.ispartofseries.pt-BR.fl_str_mv v. 160, p. 65- 76, set. 2015
dc.rights.driver.fl_str_mv Elsevier Ltd.
info:eu-repo/semantics/openAccess
rights_invalid_str_mv Elsevier Ltd.
eu_rights_str_mv openAccess
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dc.publisher.none.fl_str_mv Journal of Food Engineering
publisher.none.fl_str_mv Journal of Food Engineering
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