Friction losses in valves and fittings for power-law fluids

Detalhes bibliográficos
Autor(a) principal: Polizelli, M.A. [UNESP]
Data de Publicação: 2003
Outros Autores: Menegalli, F.C., Telis, V.R.N. [UNESP], Telis-Romero, J. [UNESP]
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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spelling 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
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