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Three-dimensional flow around and through a porous screen

Published online by Cambridge University Press:  16 May 2024

Olivier C. Marchand*
Affiliation:
Laboratoire d'Hydrodynamique (LadHyX), UMR7646, CNRS, École polytechnique, Institut Polytechnique de Paris, 91120 Palaiseau, France
Sophie Ramananarivo
Affiliation:
Laboratoire d'Hydrodynamique (LadHyX), UMR7646, CNRS, École polytechnique, Institut Polytechnique de Paris, 91120 Palaiseau, France
Camille Duprat
Affiliation:
Laboratoire d'Hydrodynamique (LadHyX), UMR7646, CNRS, École polytechnique, Institut Polytechnique de Paris, 91120 Palaiseau, France
Christophe Josserand
Affiliation:
Laboratoire d'Hydrodynamique (LadHyX), UMR7646, CNRS, École polytechnique, Institut Polytechnique de Paris, 91120 Palaiseau, France
*
Email address for correspondence: olivier.marchand@ladhyx.polytechnique.fr

Abstract

We investigate the three-dimensional (3-D) flow around and through a porous screen for various porosities at high Reynolds number $Re = {O}(10^4)$. Historically, the study of this problem has been focused on two-dimensional cases and for screens spanning completely or partially a channel. Since many recent problems have involved a porous object in a 3-D free flow, we present a 3-D model initially based on Koo & James (J. Fluid Mech., vol. 60, 1973, pp. 513–538) and Steiros & Hultmark (J. Fluid Mech., vol. 853, 2018 pp. 1–11) for screens of arbitrary shapes. In addition, we include an empirical viscous correction factor accounting for viscous effects in the vicinity of the screen. We characterize experimentally the aerodynamic drag coefficient for a porous square screen composed of fibres, immersed in a laminar air flow with various solidities and different angles of attack. We test various fibre diameters to explore the effect of the space between the pores on the drag force. Using PIV and hot wire probe measurements, we visualize the flow around and through the screen, and in particular measure the proportion of fluid that is deviated around the screen. The predictions from the model for drag coefficient, flow velocities and streamlines are in good agreement with our experimental results. In particular, we show that local viscous effects are important: at the same solidity and with the same air flow, the drag coefficient and the flow deviations strongly depend on the Reynolds number based on the fibre diameter. The model, taking into account 3-D effects and the shape of the porous screen, and including an empirical viscous correction factor that is valid for fibrous screens may have many applications including the prediction of water collection efficiency for fog harvesters.

Type
JFM Papers
Copyright
© The Author(s), 2024. Published by Cambridge University Press

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