Hostname: page-component-7b7567c8c-kwt9d Total loading time: 0 Render date: 2026-11-14T07:56:55.187Z Has data issue: false hasContentIssue false

Poiseuille and thermal transpiration flows of a dense gas between two parallel plates

Published online by Cambridge University Press:  03 May 2023

Masanari Hattori*
Affiliation:
Department of Aeronautics and Astronautics, Graduate School of Engineering, Kyoto University, Kyoto 615-8540, JapanResearch Project of Fluid Science and Engineering, Advanced Engineering Research Center, Kyoto University, Kyoto 615-8540, Japan
*
†Email address for correspondence: hattori.masanari.4r@kyoto-u.ac.jp

Abstract

The Poiseuille and thermal transpiration flows of a dense gas between two parallel plates are investigated on the basis of the Enskog kinetic equation under the diffuse reflection boundary condition. In contrast to the case of an ideal gas, the density and the gradients of pressure and the normal stress component in the flow direction are not uniform in the direction normal to the plates for a dense gas. The non-uniform normal stress gradient contributes also to the acceleration or deceleration of the thermal transpiration flow for small Knudsen numbers. The profiles of mass and heat flows as well as the net mass flows are obtained for various Knudsen numbers and ratios of the molecular diameter to the distance of plates. In the analysis of the Poiseuille flow, most characteristics of a force-driven flow with a small force are recovered. However, for the case of a dense gas, differences between the force-driven and the present pressure-driven flows are observed even within the linearized regime for small force and pressure gradient, especially at the microscopic level. The behaviour of the velocity distribution functions, in particular, the way in which they approach the ones for the Boltzmann equation as the molecular diameter becomes smaller, is clarified.

Information

Type
JFM Papers
Copyright
© The Author(s), 2023. Published by Cambridge University Press
Figure 0

Figure 1.Plot of the volume fraction of molecules $\eta _{0}$ as a function of $k$ for $\hat {\sigma } = 0.001$, $0.01$, $0.05$, $0.1$ and $0.15$.

Figure 1

Figure 2.Profiles of quantities related to the density and the gradients of the pressure and the $(2,2)$ component of stress; (a) $\hat {\rho }_{M}$, (b) $\hat {\omega }_{T}$ and $\hat {\omega }_{P}$, (c) $G_{T}$, (d) $G_{{22},T}^{({k})} + G_{22,T}^{({v})}$, (e) $G_{P}$ and ( f) $G_{{22},P}^{({k})} + G_{22,P}^{({v})}$.

Figure 2

Figure 3.Deviation of densities $\hat {\rho }_{M}$ and $\hat {\omega }_{P}$ from their values at the middle of the gap; (a) $|\hat {\rho }_{M}(x_{1})-\hat {\rho }_{M}(0)|$ for $k = 0.1$, (b) $|\hat {\rho }_{M}(x_{1})-\hat {\rho }_{M}(0)|$ for $k = 1$, (c) $|\hat {\omega }_{P}(x_{1})-\hat {\omega }_{P}(0)|$ for $k = 0.1$, (d) $|\hat {\omega }_{P}(x_{1})-\hat {\omega }_{P}(0)|$ for $k = 1$, (e) $|\hat {\rho }_{M}(-(1-\hat {\sigma })/2)-\hat {\rho }_{M}(0)|/(4\eta _{0})$ and ( f) $|\hat {\omega }_{P}(-(1-\hat {\sigma })/2)-\hat {\omega }_{P}(0)|/(8\eta _{0})$. In (a–d), the quantities are plotted as functions of $(x_{1}+(1-\hat {\sigma })/2)/\hat {\sigma }$, the distance from the boundary scaled by the molecular diameter $\hat {\sigma }$. In (e, f), the quantities are scaled by the volume fraction of molecules $\eta _{0}$ and plotted as functions of $k$.

Figure 3

Figure 4.Profiles of the mass flow of the thermal transpiration flow; $\hat {\rho }_{M}u[\varPsi _{T}]$ vs $x_{1}$. (a) $k = 10$, $1$ and $0.3$, (b) $k = 0.1$, (c) $k = 0.07$ and (d) $k = 0.05$.

Figure 4

Figure 5.Profiles of the mass flow of the Poiseuille flow; $\hat {\rho }_{M}u[\varPsi _{P}]$ vs $x_{1}$. (a) $k = 10$ and $1$, (b) $k = 0.3$, (c) $k = 0.1$, (d) $k = 0.07$ and (e) $k = 0.05$.

Figure 5

Figure 6.Profiles of the heat flow of the thermal transpiration flow; $Q^{({k})}[\varPsi _{T}]+Q^{({v})}_{T}$ vs $x_{1}$; (a) $k = 10$, $1$ and $0.3$, (b) $k = 0.1$, (c) $k = 0.07$ and (d) $k = 0.05$.

Figure 6

Figure 7.Profiles of the heat flow of the Poiseuille flow; $Q^{({k})}[\varPsi _{P}]+Q^{({v})}_{P}$ vs $x_{1}$; (a) $k = 10$, $1$ and $0.3$, (b) $k = 0.1$, (c) $k = 0.07$ and (d) $k = 0.05$.

Figure 7

Figure 8.Comparison between the pressure-driven and force-driven Poiseuille flows for the mass flow, heat flow and marginal source term for $k = 0.1$; (a) $\hat {\rho }_{M}u{[}\varPsi _{P}{]}$, (b) $Q^{({k})}{[}\varPsi _{P}{]}+Q^{({v})}_{P}$, (c) $I_{P}^{{\dagger} }$ and $I_{\mathrm {F}}^{{\dagger} }$ for $\hat {\sigma } = 0.1$ and (d) $I_{P}^{{\dagger} }$ and $I_{\mathrm {F}}^{{\dagger} }$ for $\hat {\sigma } = 0.001$. In (a,b), the symbols indicate the pressure-driven case, while the solid lines the force-driven case. In (c,d), the solid lines indicate the pressure-driven case, while the dashed lines the force-driven case.

Figure 8

Figure 9.Quantities related to the net mass flows for the thermal transpiration and Poiseuille flows; (a) $\mathcal {M}_{T}$, (b) $\mathcal {M}_{P}$, (c) $\mathcal {M}_{T}/\mathcal {M}_{T,{B}}$, (d) $\mathcal {M}_{P}/\mathcal {M}_{P,{B}}$, (e) $\mathcal {M}_{T,*}$ and ( f) $\mathcal {M}_{P,*}$.

Figure 9

Figure 10.The VDF $\varPsi _{T}$ at $(\zeta _{2},\zeta _{3}) = (1.106, 0)$ for $k = 0.1$; (a) $x_{1} = -(1-\hat {\sigma })/2$, (b) close-up of (a), (c) $x_{1} = -0.25$ and (d) $x_{1} = 0$.

Figure 10

Figure 11.The VDF $\varPsi _{T}$ at $(\zeta _{2},\zeta _{3}) = (1.106, 0)$ for $k = 1$; (a) $x_{1} = -(1-\hat {\sigma })/2$, (b) close-up of (a), (c) $x_{1} = -0.25$ and (d) $x_{1} = 0$.

Figure 11

Figure 12.The VDF $\varPsi _{T}$ at $(\zeta _{2},\zeta _{3}) = (1.106, 0)$ for $k = 10$; (a) $x_{1} = -(1-\hat {\sigma })/2$, (b) close-up of (a), (c) $x_{1} = -0.25$ and (d) $x_{1} = 0$.

Figure 12

Figure 13.Plots of the collision integral $C(\varPsi _{T})$ and the collision frequency $\nu$ at $(\zeta _{2},\zeta _{3}) = (1.106, 0)$ for $k = 1$; (a) $C(\varPsi _{T})$ at $x_{1} = -(1-\hat {\sigma })/2$, (b) $C(\varPsi _{T})$ at $x_{1} = -0.25$, (c) $\nu$ at $x_{1} = -(1-\hat {\sigma })/2$, (d) $\nu$ at $x_{1} = -0.25$ and (e) $\nu$ at $\zeta _{1}= 0$.

Figure 13

Figure 14.Plots of the normalized deviation of the VDF for the Enskog equation from that for the Boltzmann equation; $\Delta \varPsi _{T}/(\Delta \varPsi _{T})|_{\zeta _{1}=-0}$ at $(\zeta _{2},\zeta _{3}) = (1.106, 0)$; (a) vs $\zeta _{1}$ and (b) vs $k\zeta _{1}/\hat {\sigma }$.