A comprehensive set of exact analytical solutions are presented describing parallel and concentric flows. Usage data cannot currently be displayed. Abstract views reflect the number of visits to the article landing page. (J Microelectromec Syst 6:167, 1997) as the channel aspect ratio approached zero. In fluid dynamics, the Hagen–Poiseuille equation, also known as the Hagen–Poiseuille law, Poiseuille law or Poiseuille equation, is a physical law that gives the pressure drop in a fluid flowing through a long cylindrical pipe. Copyright © 2020 Elsevier B.V. or its licensors or contributors. An analytical solution is derived for this case and the results are discussed. Unusual and detailed information about the rates of, An analytic expression in integral form is derived for the flow velocity in a pipe with a circular arc cross section. Section 3 is devoted to an energy analysis of the flow which proves useful when However, axisymmetric disturbances remain unstable, with critical Reynolds number tending to infinity as η → 0. We then present in Sect. These solutions are used to compare the obtained results and the corresponding exact analytical solutions. The results are used to obtain an approximate expression for the flow strength in such a pipe as a function of the size and shape of the cross section. in long, straight, and uniform rectangular microchannels in the case of different first-order slip boundary conditions on A general analytical solution is derived and the results for the latter case are discussed and the effects of the angle of the sector, the radii ratio and the slip number are … It turns out that there are three flow regimes defined by two critical values of the pressure gradient. ScienceDirect ® is a registered trademark of Elsevier B.V. ScienceDirect ® is a registered trademark of Elsevier B.V. Newtonian Poiseuille flow in ducts of annular-sector cross-sections with Navier slip. This article presents analytical expressions of velocity and mass flow rate in terms of Fourier series for gaseous slip flows Tsukahara, Takahiro Close this message to accept cookies or find out how to manage your cookie settings. We find that the flow is unstable above a critical Reynolds number for all 0 < η ≤ 1, where η is the ratio between the radii of the inner and outer cylinders. Closed form expressions for the circular and rectangular ducts are obtained. We consider the Newtonian Poiseuille flow in a duct the cross section of which is either a circular or an annular sector assuming that Navier slip occurs either along both the cylindrical walls or only along the outer cylindrical wall. The energy equation is incorporated to examine the heat transfer individualities. KeywordsGaseous slip flow-Slip boundary conditions-Rectangular microchannel-Tangential momentum accommodation coefficient (TMAC). The linear stability of flow along an annular pipe formed by two coaxial circular cylinders is considered. {\displaystyle {\begin{aligned}u(r)&={\frac {G}{4\mu }}(R_{1}^{2}-r^{2})+{\frac {G}{4\mu }}(R_{2}^{2}-R_{1}^{2}){\frac {\l… We consider the Newtonian Poiseuille flow in a duct the cross section of which is either a circular or an annular sector assuming that Navier slip occurs either along both the cylindrical walls or only along the outer cylindrical wall. Navier slip is assumed to occur along the circular walls. It is distinguished from drag-induced flow such as Couette Flow. Principal Results of Tests on Flow of Liquids in Annular Section No. Sci. This is termed as annular Poiseuille flow (aPf). Matas, Jean-Philippe An increasing number of research groups now dedicate great attention to the study of the flow of liquids at solid interfaces, and as a result a large number of experimental, computational and theoretical studies have appeared in the literature. In Sect. The outlet of the channel is carried with Neumann condition. Check if you have access via personal or institutional login, COPYRIGHT: © Cambridge University Press 2008, MathJax is a JavaScript display engine for mathematics. 2017. Other factors such as urine composition may be a major contributor to stent failure. Principal Results of Tests on Flow of Liquids in 1 -in. For several centuries fluid dynamics studies have relied upon the assumption that when a liquid flows over a solid surface, the liquid molecules adjacent to the solid are stationary relative to the solid. Symmetry means that Poiseuille flow is swirl-free and axisymmetric. It is assumed that boundary slip occurs only above a critical value of the wall shear stress, namely the slip yield stress. exactly what eq. In this paper, an exact solution of Hagen-Poiseuille flow in channels of semi-circular cross-sections is obtained as no such available in the literature. This no-slip boundary condition (BC) has been applied successfully to model many macroscopic experiments, but has no microscopic justification. Such values are recorded by adopted line integration around the outer surface of the obstacle. To be more specific, a channel of length 2.2 m and height 0.41 m is considered. The available experimental works quoted in the open literature are critically analysed in order to highlight the main results obtained on the friction factor, on the laminar-to-turbulent transition and on the Nusselt number in channels having a hydraulic diameter less than 1 mm. Deformation alone on four different levels (0°, 20°, 40°, 60°) has essentially no influence on fluid flow and renal pressure variation. Tsukahara, Takahiro In addition for more physical insight of problem velocity and pressure plots and line graphs are added. The numerical method used in this case is the finite-element method. Email your librarian or administrator to recommend adding this journal to your organisation's collection. and Due to a circular obstacle, both the drag and lift coefficients are evaluated around the outer surface of an obstacle towards the higher values of the Power law index. We express it in an equivalent but a A general analytical solution is derived for the above flow. Transitional structures in annular Poiseuille ow 3 (a) d r ri ro x (b) 0 1 0 0.5 1 h = 0.8 h = 0.5-3h = 0.3 h = 0.1 h = 10-2 h = 10 h = 10-5 ux/umax y / d Figure 1. The effects of the sector angle, the radii ratio and the slip number are analysed. The mathematical model is structured by using the fundamental laws involved in the field of fluid rheology. The Power law fluid model is carried out with Carreau–Bird law as a non-Newtonian fluid model, and both the Power law linear (constant) and parabolic velocity profiles are initiated simultaneously at an inlet of the channel. Sturm-Liouville problem different from that obtained using the static Navier slip condition. https://doi.org/10.1016/j.euromechflu.2018.05.002. In my book the flowrate Q is given as a function of the pressure gradient. Graphical trends against involved parametric variables are adorned. To read the article of this research, you can request a copy directly from the authors. It is noticed that the parabolic velocity profile at an inlet of channel is compatible as compared to the linear velocity profile. Fully developed laminar forced convection inside a semi-circular channel filled with a Brinkman-Darcy porous medium is studied. The computed first-order dimensionless Navier slip is assumed to occur along the circular walls. Can you please clarify what you mean with "hollow rectangular flow"? The method is efficient and accurate. A surface integral numerical solution for laminar developed flow in ducts of arbitrary shape cross sections is presented. Principal Results of Tests on Flow of Liquids in Annular Section No. ignored. clear fluid (s® 0s\rightarrow 0) limit are found. The Newtonian Poiseuille flow in ducts of annular-sector or circular-sector cross-sections is considered. View all Google Scholar citations In this article we consider a smooth channel with infinite length. Duguet, Yohann We consider the Newtonian Poiseuille flow in a tube whose cross-section is an equilateral triangle. A short presentation of the principle and results of molecular dynamics simulations is provided in Sect. Happel, J. and Brenner, H. (1973) Low Reynolds Number Hydrodynamics, Noordhoff, Leyden. All rights reserved. Shah, R. K. and London, A. L. (1978) Laminar flow forced convection in ducts. Poiseuille flows, in the presence of wall slip that follows a logarithmic slip law. We use cookies to help provide and enhance our service and tailor content and ads. A second asymptotic analysis is performed to show that the critical Reynolds number Rec ∝ η−1 log(η−1) as η → 0, with the form of the mean flow profile causing the appearance of the logarithm. The Newtonian Poiseuille flow in ducts of annular-sector or circular-sector cross-sections is considered. Finally, the findings are concluded with the potential remark that the flow in a channel (having no-slip condition at both the lower and upper walls) with the parabolic velocity profile initiated at the inlet is the more realistic approach as compared to the linear (constant) profile being considered at the inlet.

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