2018
DOI: 10.1007/s40819-018-0541-7
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Theoretical Study of Oldroyd-B Visco-Elastic Fluid Flow Through Curved Pipes with Slip Effects in Polymer Flow Processing

Abstract: N o r o u zi, M , D avoo di, M , B e g, OA a n d S h a m s h u d di n, M D h t t p:// dx.

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Cited by 28 publications
(18 citation statements)
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“…The present work has considered the Reiner-Rivlin third-grade non-Newtonian differential model. Future studies will consider alternative rheological models including the Oldroyd-B model [57], single-phase and two-phase Jeffery's viscoelastic models [58,59] and may also consider non-Fourier heat flux models in rheological coating heat transfer [60]. .…”
Section: Discussionmentioning
confidence: 99%
“…The present work has considered the Reiner-Rivlin third-grade non-Newtonian differential model. Future studies will consider alternative rheological models including the Oldroyd-B model [57], single-phase and two-phase Jeffery's viscoelastic models [58,59] and may also consider non-Fourier heat flux models in rheological coating heat transfer [60]. .…”
Section: Discussionmentioning
confidence: 99%
“…The current simulations have considered a no‐slip hydrodynamic wall condition for velocity. Future studies will investigate both isotropic and anisotropic hydrodynamic slip and furthermore will also address non‐Fourier heat transfer in non‐Newtonian fluids, for example, viscoelastic fluids, which are of great relevance to rotating disk bioreactor flows in chemical engineering since such systems feature complex fluids. Additionally the current study could be extended to consider variable thickness of the disk, chemical reactions, and magnetohydrodynamics when the working fluids are electrically conducting …”
Section: Discussionmentioning
confidence: 99%
“…The nondimensional ordinary differential Equations along with boundary conditions (14) are initially perturbed into a set of differential equations using the rotational Re as the perturbation parameter (Re1), following Van Dyke . Defining the expansions for each transformed variable, f , g , p and θ , we have: f=f0+Re0.25emf1+Re20.25emf2+ofalse(Re3false)g=g0+Re0.25emg1+Re20.25emg2+ofalse(Re3false)p=p0+Re0.25emp1+Re20.25emp2+ofalse(Re3false)θ=θ0+Re0.25emθ1+Re20.25emθ2+ofalse(Re3false)}.…”
Section: Pertubation Solutionmentioning
confidence: 99%
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“…Titanium nanoparticles show better results to improve lubricity and rheological features of drilling fluid at 0.6% (w/w) concentration. Viscoelastic fluid passing through the curved pipes with slip boundary conditions has been studied by Norouzi et al 6 They employed the Oldroyd-B scheme to the transport of dilute polymeric solutions in curve pipes, where Weissenberg number and slip coefficients greatly affected the viscoelastic flow. It is found that maximum velocity position changes from pipes center toward the outer side of curvature when increment occurs in slip coefficient.…”
Section: Introductionmentioning
confidence: 99%