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Pressure losses in the laminar flow of shear-thinning power-law fluids across a sudden axisymmetric expansion
A numerical investigation was carried out to study the laminar non-Newtonian flow through an axisymmetric sudden expansion having a diameter ratio of 1 to 2.6. The fluids were inelastic and shear thinning with a viscosity obeying the power law model. The recirculation length and strength and, most i...
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Published in: | The International journal of heat and fluid flow 2003-10, Vol.24 (5), p.747-761 |
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container_end_page | 761 |
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container_start_page | 747 |
container_title | The International journal of heat and fluid flow |
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creator | Pinho, F.T Oliveira, P.J Miranda, J.P |
description | A numerical investigation was carried out to study the laminar non-Newtonian flow through an axisymmetric sudden expansion having a diameter ratio of 1 to 2.6. The fluids were inelastic and shear thinning with a viscosity obeying the power law model. The recirculation length and strength and, most importantly, the local loss coefficient
C
I were quantified as a function of the inlet pipe Reynolds number and shear-thinning intensity. When using the generalised Reynolds number introduced by Metzner and Reed [AIChEJ 1 (1955) 434] (
Re
gen), at low Reynolds numbers
C
I increased by more than 100% when
n varied from 1.0 to 0.2, whereas
C
I decreased by more than 50% at high Reynolds numbers. However, this feature was shown to be related to the definition of the Reynolds number. A correlation between
C
I,
Re
gen and
n is presented at the end. |
doi_str_mv | 10.1016/S0142-727X(03)00083-3 |
format | article |
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C
I were quantified as a function of the inlet pipe Reynolds number and shear-thinning intensity. When using the generalised Reynolds number introduced by Metzner and Reed [AIChEJ 1 (1955) 434] (
Re
gen), at low Reynolds numbers
C
I increased by more than 100% when
n varied from 1.0 to 0.2, whereas
C
I decreased by more than 50% at high Reynolds numbers. However, this feature was shown to be related to the definition of the Reynolds number. A correlation between
C
I,
Re
gen and
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C
I were quantified as a function of the inlet pipe Reynolds number and shear-thinning intensity. When using the generalised Reynolds number introduced by Metzner and Reed [AIChEJ 1 (1955) 434] (
Re
gen), at low Reynolds numbers
C
I increased by more than 100% when
n varied from 1.0 to 0.2, whereas
C
I decreased by more than 50% at high Reynolds numbers. However, this feature was shown to be related to the definition of the Reynolds number. A correlation between
C
I,
Re
gen and
n is presented at the end.</description><subject>Exact sciences and technology</subject><subject>Flows in ducts, channels, nozzles, and conduits</subject><subject>Fluid dynamics</subject><subject>Fundamental areas of phenomenology (including applications)</subject><subject>Non-newtonian fluid flows</subject><subject>Physics</subject><subject>Pressure loss</subject><subject>Recirculation length</subject><subject>Shear thinning</subject><subject>Sudden expansion</subject><issn>0142-727X</issn><issn>1879-2278</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2003</creationdate><recordtype>article</recordtype><recordid>eNqFkE9r3DAQxUVoINttPkJBl5b24HYk2SvtqZSQ_oFAAm2gNyFL466KLbsaO7v59rV3Q3vsaRj4vXnzHmMvBbwTIDbvv4EoZaGl_vEG1FsAMKpQZ2wljN4WUmrzjK3-IhfsOdGvGdpAqVesu8tINGXkbU-ExGPi427eXBeTy7xp-z3vG047dLkYdzGlmH7yod9jLlq3n4EpBuLO51nPHacpBEzcHSI9dh2OOXqOh8Elin16wc4b1xJePs01u_90_f3qS3Fz-_nr1cebwquNGQvtBdTSyLoMYLz02yYoIbbabyTWpTRaeJClC6IxrhahlrrCAI0CUEsuo9bs9enukPvfE9Jou0ge29Yl7CeyUm-lrMoFrE7g8f2MjR1y7Fx-tALsUq49lmuX5iwoeyzXqln36snAkXdtk13ykf6JK6E0VAv34cThnPYhYrbkIyaPIWb0ow19_I_TH7jFj_s</recordid><startdate>20031001</startdate><enddate>20031001</enddate><creator>Pinho, F.T</creator><creator>Oliveira, P.J</creator><creator>Miranda, J.P</creator><general>Elsevier Inc</general><general>Elsevier Science</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>7TB</scope><scope>8FD</scope><scope>FR3</scope></search><sort><creationdate>20031001</creationdate><title>Pressure losses in the laminar flow of shear-thinning power-law fluids across a sudden axisymmetric expansion</title><author>Pinho, F.T ; Oliveira, P.J ; Miranda, J.P</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c368t-7c10b282b4d08c2c9fd31197c62eb42871c024ad1f8ab1db275ed0f3003006083</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2003</creationdate><topic>Exact sciences and technology</topic><topic>Flows in ducts, channels, nozzles, and conduits</topic><topic>Fluid dynamics</topic><topic>Fundamental areas of phenomenology (including applications)</topic><topic>Non-newtonian fluid flows</topic><topic>Physics</topic><topic>Pressure loss</topic><topic>Recirculation length</topic><topic>Shear thinning</topic><topic>Sudden expansion</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Pinho, F.T</creatorcontrib><creatorcontrib>Oliveira, P.J</creatorcontrib><creatorcontrib>Miranda, J.P</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Technology Research Database</collection><collection>Engineering Research Database</collection><jtitle>The International journal of heat and fluid flow</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Pinho, F.T</au><au>Oliveira, P.J</au><au>Miranda, J.P</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Pressure losses in the laminar flow of shear-thinning power-law fluids across a sudden axisymmetric expansion</atitle><jtitle>The International journal of heat and fluid flow</jtitle><date>2003-10-01</date><risdate>2003</risdate><volume>24</volume><issue>5</issue><spage>747</spage><epage>761</epage><pages>747-761</pages><issn>0142-727X</issn><eissn>1879-2278</eissn><coden>IJHFD2</coden><abstract>A numerical investigation was carried out to study the laminar non-Newtonian flow through an axisymmetric sudden expansion having a diameter ratio of 1 to 2.6. The fluids were inelastic and shear thinning with a viscosity obeying the power law model. The recirculation length and strength and, most importantly, the local loss coefficient
C
I were quantified as a function of the inlet pipe Reynolds number and shear-thinning intensity. When using the generalised Reynolds number introduced by Metzner and Reed [AIChEJ 1 (1955) 434] (
Re
gen), at low Reynolds numbers
C
I increased by more than 100% when
n varied from 1.0 to 0.2, whereas
C
I decreased by more than 50% at high Reynolds numbers. However, this feature was shown to be related to the definition of the Reynolds number. A correlation between
C
I,
Re
gen and
n is presented at the end.</abstract><cop>New York, NY</cop><pub>Elsevier Inc</pub><doi>10.1016/S0142-727X(03)00083-3</doi><tpages>15</tpages></addata></record> |
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subjects | Exact sciences and technology Flows in ducts, channels, nozzles, and conduits Fluid dynamics Fundamental areas of phenomenology (including applications) Non-newtonian fluid flows Physics Pressure loss Recirculation length Shear thinning Sudden expansion |
title | Pressure losses in the laminar flow of shear-thinning power-law fluids across a sudden axisymmetric expansion |
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