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Time-dependent modelling of thin poroelastic films drying on deformable plates

Published online by Cambridge University Press:  12 April 2023

Matthew G. Hennessy*
Affiliation:
Department of Engineering Mathematics, University of Bristol, University Walk, Bristol, BS8 1TW, UK
Richard V. Craster
Affiliation:
Department of Mathematics, Imperial College London, South Kensington Campus, London, SW7 2AZ, UK
Omar K. Matar
Affiliation:
Department of Chemical Engineering, Imperial College London, South Kensington Campus, London, SW7 2AZ, UK
*
*Correspondence author. Email: matthew.hennessy@bristol.ac.uk
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Abstract

Understanding the generation of mechanical stress in drying, particle-laden films is important for a wide range of industrial processes. One way to study these stresses is through the cantilever experiment, whereby a thin film is deposited onto the surface of a thin plate that is clamped at one end to a wall. The stresses that are generated in the film during drying are transmitted to the plate and drive bending. Mathematical modelling enables the film stress to be inferred from measurements of the plate deflection. The aim of this paper is to present simplified models of the cantilever experiment that have been derived from the time-dependent equations of continuum mechanics using asymptotic methods. The film is described using nonlinear poroelasticity and the plate using nonlinear elasticity. In contrast to Stoney-like formulae, the simplified models account for films with non-uniform thickness and stress. The film model reduces to a single differential equation that can be solved independently of the plate equations. The plate model reduces to an extended form of the Föppl-von Kármán (FvK) equations that accounts for gradients in the longitudinal traction acting on the plate surface. Consistent boundary conditions for the FvK equations are derived by resolving the Saint-Venant boundary layers at the free edges of the plate. The asymptotically reduced models are in excellent agreement with finite element solutions of the full governing equations. As the Péclet number increases, the time evolution of the plate deflection changes from $t$ to $t^{1/2}$, in agreement with experiments.

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Papers
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This is an Open Access article, distributed under the terms of the Creative Commons Attribution licence (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted re-use, distribution and reproduction, provided the original article is properly cited.
Copyright
© The Author(s), 2023. Published by Cambridge University Press
Figure 0

Figure 1. Bending of a plate during film drying. The plate has length $L$, width $W$ and height $H_p$. The initial film thickness is given by $H_f(X_1, X_2)$, where $X_1$ and $X_2$ are Lagrangian coordinates that lie in the plane spanned by the plate centreline (dashed line). The plate is clamped to a wall at $X_1 = 0$. The origin of the vertical Lagrangian coordinate $Z$ coincides with the plate centreline. Panels (a) and (b): Cross-sections of the Lagrangian (undeformed) configuration. Panel (c): Cross-section of the Eulerian (deformed) configuration.

Figure 1

Figure 2. Finite element simulations of the film-plate model presented in Sec. 2. The heat map represents the Eulerian fluid fraction (porosity) of the film, $\phi = \Phi / J$. Simulation snapshots are shown at times (a) $t = 0$, (b) $t = 0.005$, (c) $t = 0.010$, (d) $t = 0.015$, (e) $t = 0.020$, and (f) $t = 0.025$. The parameter values are $\epsilon = \delta = 0.1$, $\textrm{Pe} = 100$, $\varepsilon = 3$ with $\phi_0 = 0.68$, and $k(\phi) \equiv 1$. The non-dimensional evaporative flux is $\mathcal{V}(\phi) = \phi - \phi_\infty$, where $\phi_\infty = 0.36$.

Figure 2

Figure 3. Steady-state solutions of the vertical plate displacement when the film and plate have similar thicknesses, $\delta = O(\epsilon)$ with $\mathcal{E} = O(1)$. Asymptotic solutions are shown as lines and obtained from (6.2); finite element solutions are shown as symbols. (a) The deflection at the end of the plate as a function of the imposed (uniform) contraction ratio J in the film. (b) The vertical displacement of the plate as a function of space when $J = 0.2$.

Figure 3

Figure 4. Steady-state solutions when the film is thin relative to the plate, $\epsilon \ll \delta$. Asymptotic solutions are shown as lines; finite element solutions are shown as symbols. (a) The deflection at the end of the plate as a function of the imposed (uniform) contraction ratio J in the film. The asymptotic solution for w is obtained from (6.2) with $\epsilon \delta^{-1} = 0$. (b) The vertical traction $\tau_z$ as a function of space. The asymptotic solutions for the traction are given by (5.21b) when $\mathcal{E} = 1$ and (5.22) when $\mathcal{E} = 10$.

Figure 4

Figure 5. Drying dynamics for small evaporation rates, $\textrm{Pe} = O(1)$, when the film and plate have similar thicknesses, $\delta = O(\epsilon)$. Asymptotic solutions are shown as lines; finite element solutions are shown as circles. (a) The Eulerian fluid fraction at the bottom of the film. (b) and (c) The in-plane and vertical traction. (d) The vertical plate displacement. The inset shows the evolution of the deflection of the end of the plate. Solutions are shown at times $t = 0.1$, 0.4, 0.7, 1, and 3. The arrows show the direction of increasing time. The parameter values are $\epsilon = \delta = 0.01$, $\textrm{Pe} = 1$, and $\mathcal{E} = 1$.

Figure 5

Figure 6. Drying dynamics for moderate evaporation rates, $\textrm{Pe} = O(\epsilon^{-1})$, when the film and plate have similar thicknesses, $\delta = O(\epsilon)$. Asymptotic solutions are shown as lines; finite element solutions are shown as circles. (a) The Eulerian fluid fraction at the bottom of the film. (b) and (c) The in-plane and vertical traction. (d) The vertical plate displacement. The inset shows the evolution of the deflection of the end of the plate. Solutions are shown at times $t = 0.001$, 0.005, 0.01, 0.02, and 0.05. The arrows show the direction of increasing time. The parameter values are $\epsilon = \delta = 0.01$, $\textrm{Pe} = 100$, and $\mathcal{E} = 1$.

Figure 6

Figure 7. Drying dynamics for large evaporation rates, $\textrm{Pe} = O(\epsilon^{-2})$, when the film is much thinner than the plate, $\epsilon \ll \delta$. Asymptotic solutions are shown as lines; finite element solutions are shown as circles. (a) The Eulerian fluid fraction at the bottom of the film. (b) The vertical plate displacement. The inset shows the evolution of the deflection of the end of the plate. (c) and (d) The Eulerian fluid fraction and in-plane film stress at the centre of the film. Solutions are shown at times $t = 2 \times 10^{-6}$, $10^{-5}$, $2 \times 10^{-5}$, $4 \times 10^{-5}$, and $10^{-4}$. The arrows show the direction of increasing time. The parameter values are $\epsilon = 0.01$, $\delta = 0.1$, $\textrm{Pe} = 5 \times 10^{4}$, and $\mathcal{E} = 1$.

Figure 7

Figure 8. (a) Asymptotic solutions for plate deflection plotted in terms of $\textrm{Pe}\, t$ for five different drying regimes. (b) Asymptotic solutions for the in-plane traction when $\textrm{Pe} = 1$ (top) and $\textrm{Pe} = \epsilon ^{-2}$ (bottom). The solutions are shown when $\textrm{Pe}\, t = 0.1$, $0.3$ and $0.6$. The arrows show the direction of increasing time. See text for full details.