Abstract:The paper presents a numerical investigation of non-Newtonian modeling effects on unsteady periodic flows in a two-dimensional (2D) constricted channel with moving wall using finite volume method. The governing Navier-Stokes equations have been modified using the Cartesian curvilinear coordinates to handle complex geometries, such as, arterial stenosis. The physiological pulsatile flow has been used at the inlet position as an inlet velocity. The flow is characterized by the Reynolds numbers 300, 500, and 750 … Show more
“…The idea of using viscosity distribution function as appears in (25) is due to the theoretical and experimental results of blood viscosity behavior that obtained by Cerny and Walawender [4] and Pontrelli [44] and many others [39][40][41][42][43][44][45][46][47][48][49][50][51][52][53][54] as appear in…”
Section: Newtonian Fluid =mentioning
confidence: 99%
“…Likewise the Newtonian case, it is easy to deduce from Equation (2) that also the non-Newtonian velocity is decreased with the radial distance increase which also fits with the literature results. [5,44,[46][47][48][49][50]52,53] Also, the value of has a significant impact on the Newtonian fluid according to [56]. In addition, the effect of the wedge semiangle ( ) on the velocity ( ) is not 'tolerable' (92%) when comparing the error between the approximate and the numerical solutions, i.e., while increasing the angle from = 1 0 to = 10 0 so that assumption (61) for 2 ≪ 1 is no longer valid.…”
Section: Non-newtonian Fluid =mentioning
confidence: 99%
“…[50,51] However, excluding some points of distinction these assumptions are still valid and are well supported by literature. [52] Some other limited configurations like vertical channel [53] and even different cross section channels [54] have shown similar velocity behavior in the qualitative aspect. Different pressure modeling types (axial and hydrostatic pressures distribution) are examined and discussed in the present study.…”
Section: Introductionmentioning
confidence: 99%
“…Analytic analysis will be performed for small and high semi-wedge angles with various friction coefficients. The results will be compared qualitatively with the available literature data information [44][45][46][47][48][49][50][51][52][53][54] and hopefully, contribute to the biomed and polymer scientific areas.…”
The radial planar wedge pattern flow with friction and normalized non-uniform viscosity function will be discussed here. Solving this problem will be done using the flow theory equations for Newtonian and Non-Newtonian cases with non-uniform viscosity assumption. General differential equation that connects between the normalized velocity profile and the normalized viscosity has been derived analytically from the flow equations. It was found that for specific wedge semi angle, the radial assumption is no longer valid for the flow velocity. Moreover, it was found that for inlet/outlet conditions the normalized mean hydrostatic pressure for Newtonian fluid is dependent on the geometry, the normalized velocity and the viscosity functions. In addition, it was found that inertia phenomenon can be neglected for small wedge semi angle. A comparison between the axial and the hydrostatic pressure distributions for inlet/outlet conditions was performed for Newtonian and non-Newtonian flows. Finally, it was found that the axial pressure distribution profile was converged to the hydrostatic profile for critical wedge semi angle.
K E Y W O R D Sblood flow, hydrostatic pressure difference, non-linear viscosity, non-Newtonian fluid, viscosity, wedge
“…The idea of using viscosity distribution function as appears in (25) is due to the theoretical and experimental results of blood viscosity behavior that obtained by Cerny and Walawender [4] and Pontrelli [44] and many others [39][40][41][42][43][44][45][46][47][48][49][50][51][52][53][54] as appear in…”
Section: Newtonian Fluid =mentioning
confidence: 99%
“…Likewise the Newtonian case, it is easy to deduce from Equation (2) that also the non-Newtonian velocity is decreased with the radial distance increase which also fits with the literature results. [5,44,[46][47][48][49][50]52,53] Also, the value of has a significant impact on the Newtonian fluid according to [56]. In addition, the effect of the wedge semiangle ( ) on the velocity ( ) is not 'tolerable' (92%) when comparing the error between the approximate and the numerical solutions, i.e., while increasing the angle from = 1 0 to = 10 0 so that assumption (61) for 2 ≪ 1 is no longer valid.…”
Section: Non-newtonian Fluid =mentioning
confidence: 99%
“…[50,51] However, excluding some points of distinction these assumptions are still valid and are well supported by literature. [52] Some other limited configurations like vertical channel [53] and even different cross section channels [54] have shown similar velocity behavior in the qualitative aspect. Different pressure modeling types (axial and hydrostatic pressures distribution) are examined and discussed in the present study.…”
Section: Introductionmentioning
confidence: 99%
“…Analytic analysis will be performed for small and high semi-wedge angles with various friction coefficients. The results will be compared qualitatively with the available literature data information [44][45][46][47][48][49][50][51][52][53][54] and hopefully, contribute to the biomed and polymer scientific areas.…”
The radial planar wedge pattern flow with friction and normalized non-uniform viscosity function will be discussed here. Solving this problem will be done using the flow theory equations for Newtonian and Non-Newtonian cases with non-uniform viscosity assumption. General differential equation that connects between the normalized velocity profile and the normalized viscosity has been derived analytically from the flow equations. It was found that for specific wedge semi angle, the radial assumption is no longer valid for the flow velocity. Moreover, it was found that for inlet/outlet conditions the normalized mean hydrostatic pressure for Newtonian fluid is dependent on the geometry, the normalized velocity and the viscosity functions. In addition, it was found that inertia phenomenon can be neglected for small wedge semi angle. A comparison between the axial and the hydrostatic pressure distributions for inlet/outlet conditions was performed for Newtonian and non-Newtonian flows. Finally, it was found that the axial pressure distribution profile was converged to the hydrostatic profile for critical wedge semi angle.
K E Y W O R D Sblood flow, hydrostatic pressure difference, non-linear viscosity, non-Newtonian fluid, viscosity, wedge
“…Rabby et al (2014) studied the Newtonian laminar fluid flow in an axisymmetric stenosis for the Reynolds number Re = 300 with a mild oscillating wall. Later on, Shupti et al (2015) have investigated the non-Newtonian fluid flow behavior through a single stenosis of maximum 60% area reduction with moving wall. In the presence of a single stenosis, for the higher Reynolds number, the flow becomes asymmetric that leads them to do further studies couples with stenosis and aneurysm.…”
This research presents a numerical simulation of an unsteady two-dimensional channel flow of Newtonian and some non-Newtonian fluids using the finite-volume method. The walls of the geometry oscillate sinusoidally with time. We have used the Cartesian curvilinear coordinates to handle complex geometries, i.e., arterial stents and bulges and the governing Navier-Stokes equations have been modified accordingly. Physiological pulsatile flow has been used at the inlet to characterize four different non-Newtonian models, i.e., the (i) Carreau, (ii) Cross, (iii) Modified Casson, and (iv) Quemada. We have presented the numerical results in terms of wall shear stress (WSS), pressure distribution as well as the streamlines and discussed the hemodynamic behaviors for laminar and laminar to turbulent transitional flow conditions. An increase of wall shear stress and a decrease in wall pressure are significantly observed at the stenosis throat for high Reynolds number and highly stenosed arteries. Likewise, the flow recirculation also increases if the narrowing level and the Reynolds number increases in the dilated region which eventually leads the stream to experience a transition to turbulence at Re = 750. The results for the fluid flow through an aneurysm just after a stenosis with oscillating wall are novel in the literature.
In this work, a stabilized time Discontinuous Galerkin, Space‐Time Finite Element (tDG‐ST‐FE) scheme is presented for discretizing time‐dependent viscous shear‐thinning fluid flow models, which exhibit a usual power‐law stress strain relation. The development of the proposed numerical scheme based mainly on a unified weak space‐time formulation, where simple streamline‐upwind terms have been added in the numerical scheme, for stabilizing the discretization of the associated temporal and convective terms. The original time interval is partitioned into time subintervals, resulting in a subdivision of the space‐time cylinder into space‐time subdomains. Discontinuous Galerkin techniques are applied for the time discretization between the space‐time subdomain interfaces. A stability bound is given for the derived ST‐FE scheme. In the last part numerical examples on benchmark problems are presented for testing the efficiency of the proposed method.
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