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Knudsen minimum disappearance in molecular-confined flows

Published online by Cambridge University Press:  25 July 2022

Carlos Corral-Casas
Affiliation:
Institute for Multiscale Thermofluids, School of Engineering, The University of Edinburgh, Edinburgh EH9 3FB, UK
Jun Li
Affiliation:
Center for Integrative Petroleum Research, College of Petroleum Engineering and Geosciences, King Fahd University of Petroleum and Minerals, Dhahran 31261, Saudi Arabia
Matthew K. Borg
Affiliation:
Institute for Multiscale Thermofluids, School of Engineering, The University of Edinburgh, Edinburgh EH9 3FB, UK
Livio Gibelli*
Affiliation:
Institute for Multiscale Thermofluids, School of Engineering, The University of Edinburgh, Edinburgh EH9 3FB, UK
*
†Email address for correspondence: livio.gibelli@ed.ac.uk

Abstract

It is well known that the Poiseuille mass flow rate along microchannels shows a stationary point as the fluid density decreases, referred to as the Knudsen minimum. Surprisingly, if the flow characteristic length is comparable to the molecular size, the Knudsen minimum disappears, as reported for the first time by Wu et al. (J. Fluid Mech., vol. 794, 2016, pp. 252–266). However, there is still no fundamental understanding why the mass flow rate monotonically increases throughout the entire range of flow regimes. Although diffusion is believed to dominate the fluid transport at the nanoscale, here we show that the Fick's first law fails in capturing this behaviour, and so diffusion alone is insufficient to explain this confined flow phenomenon. Rather, we show that the Knudsen minimum disappears in tight confinements because the decay of the mass flow rate due to the decreasing density effects is overcome by the enhancing contribution to the flow provided by the fluid velocity slip at the wall.

Information

Type
JFM Papers
Creative Commons
Creative Common License - CCCreative Common License - BY
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), 2022. Published by Cambridge University Press
Figure 0

Figure 1. (a) Comparison between the dimensionless MFR provided by non-equilibrium simulations (symbols) and the theoretical predictions assuming Fickian diffusion, as given by (3.1) (lines). There is good agreement in the free molecular regime ($Kn\geqslant 10$), whilst Fick's law underestimates MFR elsewhere, which implies that convective transport terms cannot be neglected at any confinement. The normalising factor of the MFR $\dot {m}_n$ is presented in (A6) of Appendix A. (b) Dependence of the self-diffusivity $D$ on the Knudsen number $Kn$ and the confinement ratio $R$. Horizontal lines represent the theoretical value of the Knudsen self-diffusivity from (3.2) for each confinement ratio.

Figure 1

Figure 2. (a) Qualitative analysis of the dimensionless MFR curves against the Knudsen number. In sufficiently large channels (orange colour), where the continuum transport is larger than the free molecular one, the MFR curve develops two stationary points. In tighter confinements (blue colour), where the free molecular flow is larger than the continuum one, the MFR curve could either show the two stationary points or follow a monotonic increase instead, where the Knudsen minimum disappears. (b) Relative percentage error of the MFR predicted by the Navier–Stokes equation with slip, for different confinement ratios. Dashed horizontal lines are the average percentage error over the displayed range of $Kn$: the mean error is within 8 % for the tighter $R=5$, whereas it reduces to less than 4 % for the largest $R=50$ considered here. The inset shows the slip coefficients determined from EDMD simulations, for different $R$ and $\eta$ values, obtained by fitting the quadratic velocity profiles.

Figure 2

Figure 3. (a) Partial rates of change against the reduced specific volume, for $R=20$, under the continuum framework of fluid modelling, which capture how flow transport is affected by a change of each of the underlying contributions. (b) Interplay between the continuum (dash-dotted) and the slip (dotted) contributions for different $R$. For sufficiently large $R$ values, the continuum contribution dominates and the sum of all rates of change (solid) crosses the $x$-axis, i.e. the Knudsen maximum appears. However, for tight channels, the continuum contribution is less relevant whereas slip remains the same, driving the overall rate of change to be positive throughout the entire range of $\nu$ values, with the Knudsen maximum disappearing as a consequence.