Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tube
Autor(a) principal: | |
---|---|
Data de Publicação: | 2011 |
Outros Autores: | , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Repositório Institucional da UNESP |
Texto Completo: | http://dx.doi.org/10.1590/S1678-58782011000300007 http://hdl.handle.net/11449/226642 |
Resumo: | This work presents a mathematical modeling to study the ester oil ISO VG-10-refrigerant R134a mixture two-phase flow with foam formation through a 3.22 mm ID tube. Based on experimental visualization results, the flow is divided into three regions: a single phase flow at the inlet of the tube; an intermediary bubbly flow region; and a foam flow region at the end of the tube. Numerical results for mass flow rate, pressure and temperature distributions along the flow were compared with experimental data available in literature, showing good agreement. The major discrepancy between the mass flow rate data was about 21%. These results show that the mathematical modeling worked well for predicting the overall characteristics of the flow and can be generically used to other oil-refrigerant mixtures. |
id |
UNSP_1a947097e9a53b51dd694ad190cb74f6 |
---|---|
oai_identifier_str |
oai:repositorio.unesp.br:11449/226642 |
network_acronym_str |
UNSP |
network_name_str |
Repositório Institucional da UNESP |
repository_id_str |
2946 |
spelling |
Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tubeCompressorFoamMixtureOilRefrigerantThis work presents a mathematical modeling to study the ester oil ISO VG-10-refrigerant R134a mixture two-phase flow with foam formation through a 3.22 mm ID tube. Based on experimental visualization results, the flow is divided into three regions: a single phase flow at the inlet of the tube; an intermediary bubbly flow region; and a foam flow region at the end of the tube. Numerical results for mass flow rate, pressure and temperature distributions along the flow were compared with experimental data available in literature, showing good agreement. The major discrepancy between the mass flow rate data was about 21%. These results show that the mathematical modeling worked well for predicting the overall characteristics of the flow and can be generically used to other oil-refrigerant mixtures.Federal University of Santa Catarina Department of Mechanical Engineering, 88040-900 Florianópolis, SCSão Paulo State University College of Ilha Solteira Department of Mechanical Engineering, 15385-000 Ilha Solteira, SPSão Paulo State University College of Ilha Solteira Department of Mechanical Engineering, 15385-000 Ilha Solteira, SPUniversidade Federal de Santa Catarina (UFSC)Universidade Estadual Paulista (UNESP)Dias, João PauloGasche, José Luiz [UNESP]Seixlack, André Luiz [UNESP]2022-04-29T02:16:59Z2022-04-29T02:16:59Z2011-01-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article314-323http://dx.doi.org/10.1590/S1678-58782011000300007Journal of the Brazilian Society of Mechanical Sciences and Engineering, v. 33, n. 3, p. 314-323, 2011.1806-36911678-5878http://hdl.handle.net/11449/22664210.1590/S1678-587820110003000072-s2.0-83455180080Scopusreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengJournal of the Brazilian Society of Mechanical Sciences and Engineeringinfo:eu-repo/semantics/openAccess2024-07-04T20:06:14Zoai:repositorio.unesp.br:11449/226642Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T17:40:44.885589Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false |
dc.title.none.fl_str_mv |
Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tube |
title |
Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tube |
spellingShingle |
Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tube Dias, João Paulo Compressor Foam Mixture Oil Refrigerant |
title_short |
Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tube |
title_full |
Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tube |
title_fullStr |
Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tube |
title_full_unstemmed |
Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tube |
title_sort |
Mathematical modeling of the ester oil-refrigerant R134a mixture two-phase flow with foam formation through a small diameter tube |
author |
Dias, João Paulo |
author_facet |
Dias, João Paulo Gasche, José Luiz [UNESP] Seixlack, André Luiz [UNESP] |
author_role |
author |
author2 |
Gasche, José Luiz [UNESP] Seixlack, André Luiz [UNESP] |
author2_role |
author author |
dc.contributor.none.fl_str_mv |
Universidade Federal de Santa Catarina (UFSC) Universidade Estadual Paulista (UNESP) |
dc.contributor.author.fl_str_mv |
Dias, João Paulo Gasche, José Luiz [UNESP] Seixlack, André Luiz [UNESP] |
dc.subject.por.fl_str_mv |
Compressor Foam Mixture Oil Refrigerant |
topic |
Compressor Foam Mixture Oil Refrigerant |
description |
This work presents a mathematical modeling to study the ester oil ISO VG-10-refrigerant R134a mixture two-phase flow with foam formation through a 3.22 mm ID tube. Based on experimental visualization results, the flow is divided into three regions: a single phase flow at the inlet of the tube; an intermediary bubbly flow region; and a foam flow region at the end of the tube. Numerical results for mass flow rate, pressure and temperature distributions along the flow were compared with experimental data available in literature, showing good agreement. The major discrepancy between the mass flow rate data was about 21%. These results show that the mathematical modeling worked well for predicting the overall characteristics of the flow and can be generically used to other oil-refrigerant mixtures. |
publishDate |
2011 |
dc.date.none.fl_str_mv |
2011-01-01 2022-04-29T02:16:59Z 2022-04-29T02:16:59Z |
dc.type.status.fl_str_mv |
info:eu-repo/semantics/publishedVersion |
dc.type.driver.fl_str_mv |
info:eu-repo/semantics/article |
format |
article |
status_str |
publishedVersion |
dc.identifier.uri.fl_str_mv |
http://dx.doi.org/10.1590/S1678-58782011000300007 Journal of the Brazilian Society of Mechanical Sciences and Engineering, v. 33, n. 3, p. 314-323, 2011. 1806-3691 1678-5878 http://hdl.handle.net/11449/226642 10.1590/S1678-58782011000300007 2-s2.0-83455180080 |
url |
http://dx.doi.org/10.1590/S1678-58782011000300007 http://hdl.handle.net/11449/226642 |
identifier_str_mv |
Journal of the Brazilian Society of Mechanical Sciences and Engineering, v. 33, n. 3, p. 314-323, 2011. 1806-3691 1678-5878 10.1590/S1678-58782011000300007 2-s2.0-83455180080 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
Journal of the Brazilian Society of Mechanical Sciences and Engineering |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
314-323 |
dc.source.none.fl_str_mv |
Scopus reponame:Repositório Institucional da UNESP instname:Universidade Estadual Paulista (UNESP) instacron:UNESP |
instname_str |
Universidade Estadual Paulista (UNESP) |
instacron_str |
UNESP |
institution |
UNESP |
reponame_str |
Repositório Institucional da UNESP |
collection |
Repositório Institucional da UNESP |
repository.name.fl_str_mv |
Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP) |
repository.mail.fl_str_mv |
|
_version_ |
1808128843602460672 |