Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurements

Bibliographic Details
Main Author: R. G. Sousa
Publication Date: 2004
Other Authors: A. M. F. R. Pinto, M. L. Riethmuller, J. B. L. M. Campos
Format: Book
Language: eng
Source: Repositórios Científicos de Acesso Aberto de Portugal (RCAAP)
Download full: https://repositorio-aberto.up.pt/handle/10216/69591
Summary: The flow around single Taylor bubbles rising in non-Newtonian solutions of Carboxymethylcellulose (CMC) polymer was studiedusing a simultaneous technique employing particle image velocimetry (PIV) and shadowgraphy. This technique solved previousproblems on finding the correct position of the bubble interface. Solutions of different polymer weight percentage, varying from0.1 to 1.0 wt% were used to cover a wide range of flow regimes. The rheological fluid properties and pipe dimension yieldedReynolds numbers between 4 and 254 and Deborah numbers between 0.012 and 0.402. The shape of the bubbles in the differentfluids was compared. The flow around the nose of the bubbles was found to be similar in all the studied conditions. Velocityprofiles in the liquid film around the bubble were measured. Different wake structures were found in the different solutionsstudied. With increasing viscosity, the wake flow varied from turbulent to laminar, being possible to observe a negative wake forthe higher polymer concentration solutions. A comparison between the different wake structures was made.
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spelling Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurementsEngenharia química, Engenharia químicaChemical engineering, Chemical engineeringThe flow around single Taylor bubbles rising in non-Newtonian solutions of Carboxymethylcellulose (CMC) polymer was studiedusing a simultaneous technique employing particle image velocimetry (PIV) and shadowgraphy. This technique solved previousproblems on finding the correct position of the bubble interface. Solutions of different polymer weight percentage, varying from0.1 to 1.0 wt% were used to cover a wide range of flow regimes. The rheological fluid properties and pipe dimension yieldedReynolds numbers between 4 and 254 and Deborah numbers between 0.012 and 0.402. The shape of the bubbles in the differentfluids was compared. The flow around the nose of the bubbles was found to be similar in all the studied conditions. Velocityprofiles in the liquid film around the bubble were measured. Different wake structures were found in the different solutionsstudied. With increasing viscosity, the wake flow varied from turbulent to laminar, being possible to observe a negative wake forthe higher polymer concentration solutions. A comparison between the different wake structures was made.20042004-01-01T00:00:00Zinfo:eu-repo/semantics/publishedVersioninfo:eu-repo/semantics/bookapplication/pdfapplication/pdfhttps://repositorio-aberto.up.pt/handle/10216/69591engR. G. SousaA. M. F. R. PintoM. L. RiethmullerJ. B. L. M. Camposinfo:eu-repo/semantics/openAccessreponame:Repositórios Científicos de Acesso Aberto de Portugal (RCAAP)instname:FCCN, serviços digitais da FCT – Fundação para a Ciência e a Tecnologiainstacron:RCAAP2025-02-27T18:48:00Zoai:repositorio-aberto.up.pt:10216/69591Portal AgregadorONGhttps://www.rcaap.pt/oai/openaireinfo@rcaap.ptopendoar:https://opendoar.ac.uk/repository/71602025-05-28T22:58:54.650053Repositórios Científicos de Acesso Aberto de Portugal (RCAAP) - FCCN, serviços digitais da FCT – Fundação para a Ciência e a Tecnologiafalse
dc.title.none.fl_str_mv Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurements
title Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurements
spellingShingle Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurements
R. G. Sousa
Engenharia química, Engenharia química
Chemical engineering, Chemical engineering
title_short Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurements
title_full Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurements
title_fullStr Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurements
title_full_unstemmed Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurements
title_sort Flow around individual Taylor bubbles rising in stagnant CMC solutions: PIV measurements
author R. G. Sousa
author_facet R. G. Sousa
A. M. F. R. Pinto
M. L. Riethmuller
J. B. L. M. Campos
author_role author
author2 A. M. F. R. Pinto
M. L. Riethmuller
J. B. L. M. Campos
author2_role author
author
author
dc.contributor.author.fl_str_mv R. G. Sousa
A. M. F. R. Pinto
M. L. Riethmuller
J. B. L. M. Campos
dc.subject.por.fl_str_mv Engenharia química, Engenharia química
Chemical engineering, Chemical engineering
topic Engenharia química, Engenharia química
Chemical engineering, Chemical engineering
description The flow around single Taylor bubbles rising in non-Newtonian solutions of Carboxymethylcellulose (CMC) polymer was studiedusing a simultaneous technique employing particle image velocimetry (PIV) and shadowgraphy. This technique solved previousproblems on finding the correct position of the bubble interface. Solutions of different polymer weight percentage, varying from0.1 to 1.0 wt% were used to cover a wide range of flow regimes. The rheological fluid properties and pipe dimension yieldedReynolds numbers between 4 and 254 and Deborah numbers between 0.012 and 0.402. The shape of the bubbles in the differentfluids was compared. The flow around the nose of the bubbles was found to be similar in all the studied conditions. Velocityprofiles in the liquid film around the bubble were measured. Different wake structures were found in the different solutionsstudied. With increasing viscosity, the wake flow varied from turbulent to laminar, being possible to observe a negative wake forthe higher polymer concentration solutions. A comparison between the different wake structures was made.
publishDate 2004
dc.date.none.fl_str_mv 2004
2004-01-01T00:00:00Z
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