2015
DOI: 10.1007/978-3-319-02426-4
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Developments in the Flow of Complex Fluids in Tubes

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Cited by 15 publications
(9 citation statements)
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References 349 publications
(681 reference statements)
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“…Yakhot and Orszag (1992) initially derived the RNG (Renormalization Group) turbulent model based on the kε turbulent model and improved it by Yakhot et al in Shih et al (1995) with scale expansions for the Reynolds stress and production of dissipation terms. Speziale and Thangam in Siginer (2015) specified that the RNG model could be a turbulence model, both for practical engineering and scientific purposes. Then, both numerical and physical 3D modeling result are analysed (Shih et al, 1995;Siginer, 2015).…”
Section: Methodsmentioning
confidence: 99%
See 1 more Smart Citation
“…Yakhot and Orszag (1992) initially derived the RNG (Renormalization Group) turbulent model based on the kε turbulent model and improved it by Yakhot et al in Shih et al (1995) with scale expansions for the Reynolds stress and production of dissipation terms. Speziale and Thangam in Siginer (2015) specified that the RNG model could be a turbulence model, both for practical engineering and scientific purposes. Then, both numerical and physical 3D modeling result are analysed (Shih et al, 1995;Siginer, 2015).…”
Section: Methodsmentioning
confidence: 99%
“…Speziale and Thangam in Siginer (2015) specified that the RNG model could be a turbulence model, both for practical engineering and scientific purposes. Then, both numerical and physical 3D modeling result are analysed (Shih et al, 1995;Siginer, 2015).…”
Section: Methodsmentioning
confidence: 99%
“…D = 1 2 (∇u+∇u T ) is the deformation rate tensor and τ p is the extra-stress tensor. In present work, the Phan-Thien-Tanner constitutive model (PTT) 38,39 is chosen to describe τ p :…”
Section: A Governing Equationsmentioning
confidence: 99%
“…It is important to emphasize the common features of and the links between three seemingly different internal flows, turbulent duct flow of Newtonian fluids, and tube flows of viscoelastic and particle laden fluids in order to help bridge the mechanics of all three, because secondary motions appear as a common thread through afore-mentioned flow types. It is not possible to develop a good understanding of the mechanics of secondary field in the flow of viscoelastic and particle laden fluids without a clear grasp of the underlying driving mechanisms of the turbulent secondary flows of Newtonian fluids [7]. At the end of this introductory paragraph on secondary motions from a broad viewpoint (fluid -geometryflow; fluid stress-strain rate relationship: Newtonian -non-Newtonian; duct centerline axis: straight -curved; duct cross-sectional shape: circular -non-circular; duct cross-sectional area/shape: constant -varying; flow configuration: external -internal; flow regime: laminarturbulent), there is an interesting fact observed in corner-flow configurations of Newtonian fluids where we encounter one of the rare cases where laminar and turbulent flows show completely different tendencies in their general behavior.…”
Section: Introductionmentioning
confidence: 99%