Friction losses in valves and fittings for power-law fluids
Autor(a) principal: | |
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Data de Publicação: | 2003 |
Outros Autores: | , , |
Tipo de documento: | Artigo |
Idioma: | eng |
Título da fonte: | Repositório Institucional da UNESP |
Texto Completo: | http://dx.doi.org/10.1590/S0104-66322003000400012 http://hdl.handle.net/11449/29925 |
Resumo: | Data on pressure drop were obtained in stainless steel, sanitary fittings and valves during laminar and turbulent flow of aqueous solutions of sucrose and xanthan gum, which were selected as model fluids. The rheological properties of these solutions were determined and the power-law model provided the best fit for experimental data. Friction losses were measured in fully and partially open butterfly and plug valves, bends and unions. Values of loss coefficients (k f) were calculated and correlated as a function of the generalized Reynolds number by the two-k method. The model adjustment was satisfactory and was better in the laminar flow range (0.976 < r² < 0.999) than in the turbulent flow range (0.774 < r² < 0.989). In order to test the adequacy of the results for predicting loss coefficients during flow of real fluids, experiments were conducted with coffee extract. Comparison between experimental and predicted loss coefficients showed very good agreement. |
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Repositório Institucional da UNESP |
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Friction losses in valves and fittings for power-law fluidsPressure dropnon-Newtonian fluidsFriction factorLoss coefficientsData on pressure drop were obtained in stainless steel, sanitary fittings and valves during laminar and turbulent flow of aqueous solutions of sucrose and xanthan gum, which were selected as model fluids. The rheological properties of these solutions were determined and the power-law model provided the best fit for experimental data. Friction losses were measured in fully and partially open butterfly and plug valves, bends and unions. Values of loss coefficients (k f) were calculated and correlated as a function of the generalized Reynolds number by the two-k method. The model adjustment was satisfactory and was better in the laminar flow range (0.976 < r² < 0.999) than in the turbulent flow range (0.774 < r² < 0.989). In order to test the adequacy of the results for predicting loss coefficients during flow of real fluids, experiments were conducted with coffee extract. Comparison between experimental and predicted loss coefficients showed very good agreement.Fundação de Amparo à Pesquisa do Estado de São Paulo (FAPESP)Universidade Estadual Paulista Departamento de Engenharia e Tecnologia de AlimentosUniversidade Estadual de Campinas Departamento de Engenharia de AlimentosUniversidade Estadual Paulista Departamento de Engenharia e Tecnologia de AlimentosBrazilian Society of Chemical EngineeringUniversidade Estadual Paulista (Unesp)Universidade Estadual de Campinas (UNICAMP)Polizelli, M.A. [UNESP]Menegalli, F.C.Telis, V.R.N. [UNESP]Telis-Romero, J. [UNESP]2014-05-20T15:16:09Z2014-05-20T15:16:09Z2003-10-01info:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/article455-463application/pdfhttp://dx.doi.org/10.1590/S0104-66322003000400012Brazilian Journal of Chemical Engineering. Brazilian Society of Chemical Engineering, v. 20, n. 4, p. 455-463, 2003.0104-6632http://hdl.handle.net/11449/2992510.1590/S0104-66322003000400012S0104-66322003000400012S0104-66322003000400012.pdf94570810881081680000-0002-2553-4629SciELOreponame:Repositório Institucional da UNESPinstname:Universidade Estadual Paulista (UNESP)instacron:UNESPengBrazilian Journal of Chemical Engineering0.9250,395info:eu-repo/semantics/openAccess2024-01-07T06:22:49Zoai:repositorio.unesp.br:11449/29925Repositório InstitucionalPUBhttp://repositorio.unesp.br/oai/requestopendoar:29462024-08-05T22:19:45.292899Repositório Institucional da UNESP - Universidade Estadual Paulista (UNESP)false |
dc.title.none.fl_str_mv |
Friction losses in valves and fittings for power-law fluids |
title |
Friction losses in valves and fittings for power-law fluids |
spellingShingle |
Friction losses in valves and fittings for power-law fluids Polizelli, M.A. [UNESP] Pressure drop non-Newtonian fluids Friction factor Loss coefficients |
title_short |
Friction losses in valves and fittings for power-law fluids |
title_full |
Friction losses in valves and fittings for power-law fluids |
title_fullStr |
Friction losses in valves and fittings for power-law fluids |
title_full_unstemmed |
Friction losses in valves and fittings for power-law fluids |
title_sort |
Friction losses in valves and fittings for power-law fluids |
author |
Polizelli, M.A. [UNESP] |
author_facet |
Polizelli, M.A. [UNESP] Menegalli, F.C. Telis, V.R.N. [UNESP] Telis-Romero, J. [UNESP] |
author_role |
author |
author2 |
Menegalli, F.C. Telis, V.R.N. [UNESP] Telis-Romero, J. [UNESP] |
author2_role |
author author author |
dc.contributor.none.fl_str_mv |
Universidade Estadual Paulista (Unesp) Universidade Estadual de Campinas (UNICAMP) |
dc.contributor.author.fl_str_mv |
Polizelli, M.A. [UNESP] Menegalli, F.C. Telis, V.R.N. [UNESP] Telis-Romero, J. [UNESP] |
dc.subject.por.fl_str_mv |
Pressure drop non-Newtonian fluids Friction factor Loss coefficients |
topic |
Pressure drop non-Newtonian fluids Friction factor Loss coefficients |
description |
Data on pressure drop were obtained in stainless steel, sanitary fittings and valves during laminar and turbulent flow of aqueous solutions of sucrose and xanthan gum, which were selected as model fluids. The rheological properties of these solutions were determined and the power-law model provided the best fit for experimental data. Friction losses were measured in fully and partially open butterfly and plug valves, bends and unions. Values of loss coefficients (k f) were calculated and correlated as a function of the generalized Reynolds number by the two-k method. The model adjustment was satisfactory and was better in the laminar flow range (0.976 < r² < 0.999) than in the turbulent flow range (0.774 < r² < 0.989). In order to test the adequacy of the results for predicting loss coefficients during flow of real fluids, experiments were conducted with coffee extract. Comparison between experimental and predicted loss coefficients showed very good agreement. |
publishDate |
2003 |
dc.date.none.fl_str_mv |
2003-10-01 2014-05-20T15:16:09Z 2014-05-20T15:16:09Z |
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/S0104-66322003000400012 Brazilian Journal of Chemical Engineering. Brazilian Society of Chemical Engineering, v. 20, n. 4, p. 455-463, 2003. 0104-6632 http://hdl.handle.net/11449/29925 10.1590/S0104-66322003000400012 S0104-66322003000400012 S0104-66322003000400012.pdf 9457081088108168 0000-0002-2553-4629 |
url |
http://dx.doi.org/10.1590/S0104-66322003000400012 http://hdl.handle.net/11449/29925 |
identifier_str_mv |
Brazilian Journal of Chemical Engineering. Brazilian Society of Chemical Engineering, v. 20, n. 4, p. 455-463, 2003. 0104-6632 10.1590/S0104-66322003000400012 S0104-66322003000400012 S0104-66322003000400012.pdf 9457081088108168 0000-0002-2553-4629 |
dc.language.iso.fl_str_mv |
eng |
language |
eng |
dc.relation.none.fl_str_mv |
Brazilian Journal of Chemical Engineering 0.925 0,395 |
dc.rights.driver.fl_str_mv |
info:eu-repo/semantics/openAccess |
eu_rights_str_mv |
openAccess |
dc.format.none.fl_str_mv |
455-463 application/pdf |
dc.publisher.none.fl_str_mv |
Brazilian Society of Chemical Engineering |
publisher.none.fl_str_mv |
Brazilian Society of Chemical Engineering |
dc.source.none.fl_str_mv |
SciELO 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_ |
1808129415615348736 |