2005
DOI: 10.1016/j.ces.2005.07.006
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Basic viscoelastic fluid flow problems using the Jeffreys model

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Cited by 25 publications
(8 citation statements)
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“…The before-mentioned fluids produce a wide range of products, such as starch suspensions, paints, thermoplastics, and so forth, which do not obey Newton's viscous law. Khadrawi et al 13 found semi-analytical solutions. Also, examined velocity and shear-type driving forces for Couette flow, transient Poiseuille, and wind-driven flow in parallel plates and a finite domain, respectively, with the impact of the Jeffrey fluid model.…”
Section: Introductionmentioning
confidence: 99%
“…The before-mentioned fluids produce a wide range of products, such as starch suspensions, paints, thermoplastics, and so forth, which do not obey Newton's viscous law. Khadrawi et al 13 found semi-analytical solutions. Also, examined velocity and shear-type driving forces for Couette flow, transient Poiseuille, and wind-driven flow in parallel plates and a finite domain, respectively, with the impact of the Jeffrey fluid model.…”
Section: Introductionmentioning
confidence: 99%
“…Polymeric liquids, colloids and many biofluids are viscoelastic [1][2][3][4][5] and exhibits extraordinary flow behaviors, not existing in Newtonian fluids, such as rod-climbing, shear thinning or pseudoplastic behavior, secondary flow in straight non-circular channels and elastic recoil [6]. Adopting appropriate constitutive equations these exotic flow behaviors can be modeled and predicted reasonably using various numerical methods [7].…”
Section: Introductionmentioning
confidence: 99%
“…Analysis of the Poiseuille flow of viscoelastic fluids has attracted noticeable attention in the past two decades for this type of flow (i) allows constitutive models to be tested under a spatially inhomogeneous deformation program, and (ii) reveals a number of interesting phenomena (melt fracture, wall slip, secondary flows) whose modeling remains a subject of debate [23][24][25][26]. Poiseuille flow has been investigated in [27][28][29] for polymer fluids described by simple differential models in nonlinear viscoelasticity, in [30] for the Wagner model, in [31,32] for the Johnson-Segalman model, in [33][34][35][36] for the Giesekus model, in [36,37] for the Leonov model, in [38] for the Phan-Thien-Tanner model, in [39,40] for the FENE model, in [41][42][43][44] for viscoelastic-plastic fluids, and in [45] for viscoelastic fluids with pressure-dependent viscosity. We concentrate on combined effects of temperature and pressure gradient on steady velocity profile.…”
Section: Introductionmentioning
confidence: 99%