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Rotational Taylor dispersion in linear flows

Published online by Cambridge University Press:  08 October 2024

Zhiwei Peng*
Affiliation:
Department of Chemical and Materials Engineering, University of Alberta, Edmonton, Alberta, Canada T6G 1H9
*
†Email address for correspondence: zhiwei.peng@ualberta.ca

Abstract

The coupling between advection and diffusion in position space can often lead to enhanced mass transport compared with diffusion without flow. An important framework used to characterize the long-time diffusive transport in position space is the generalized Taylor dispersion theory. In contrast, the dynamics and transport in orientation space remains less developed. In this work we develop a rotational Taylor dispersion theory that characterizes the long-time orientational transport of a spheroidal particle in linear flows that is constrained to rotate in the velocity-gradient plane. Similar to Taylor dispersion in position space, the orientational distribution of axisymmetric particles in linear flows at long times satisfies an effective advection–diffusion equation in orientation space. Using this framework, we then calculate the long-time average angular velocity and dispersion coefficient for both simple shear and extensional flows. Analytic expressions for the transport coefficients are derived in several asymptotic limits including nearly spherical particles, weak flow and strong flow. Our analysis shows that at long times the effective rotational dispersion is enhanced in simple shear and suppressed in extensional flow. The asymptotic solutions agree with full numerical solutions of the derived macrotransport equations and results from Brownian dynamics simulations. Our results show that the interplay between flow-induced rotations and Brownian diffusion can fundamentally change the long-time transport dynamics.

Information

Type
JFM Papers
Copyright
© The Author(s), 2024. Published by Cambridge University Press
Figure 0

Figure 1. (a) Plots of the average angular drift velocity scaled by the sphere result as a function of $Pe$ for different values of $B$. (b) Plots of the non-dimensional effective long-time dispersion coefficient as a function of $Pe$ for different values of $B$. For spheres ($B=0$), the dispersion coefficient is not affected by the flow. For non-spherical particles, shear-enhanced dispersion is observed.

Figure 1

Figure 2. Plots of numerical solutions (dashed) at $Pe=1000$ and the leading-order asymptotic solutions (dotted) at large $Pe$ for (a) the average field and (b) the displacement field. In the plots, $B=0.6$. The numerical and asymptotic solutions have excellent agreement and cannot be distinguished visually.

Figure 2

Figure 3. Plots of numerical solutions (dashed) at $Pe=1000$ and the $O(1/Pe)$ asymptotic solutions (dotted) at large $Pe$ for (a) the average field and (b) the displacement field. In the plots, $B=0.6$. The numerical approximation to $g_1$ is obtained via $g_1^{num} =Pe(g^{num} - g_0)$, where the superscript ‘$num$’ denotes a numerical solution and $g_0$ is given in (3.7a). Similarly, $b_1^{num} =Pe( b^{num} - b_0)$. The numerical and asymptotic solutions have excellent agreement and cannot be distinguished visually.

Figure 3

Figure 4. Plots of numerical solutions (circles) at $Pe=1000$ and the leading-order asymptotic solutions (dashed) at large $Pe$ for (a) the scaled drift and (b) the dispersion coefficient.

Figure 4

Figure 5. (a) Schematic of the extensional flow. (b) Schematic of the direction of rotation due to the extensional flow.

Figure 5

Figure 6. Plots of the effective dispersion coefficient as a function of $Pe\,B$ in the extensional flow. Circles are results obtained from the numerical solution of the Taylor dispersion theory, squares are results calculated from BD simulations and the dashed line denotes the leading-order asymptotic solution for small $Pe\,B$ given in (3.25).

Figure 6

Figure 7. (a) Plots of the numerical solution of $g$ (dashed) at $Pe\,B=20$ and the leading-order asymptotic solution (dotted) given in (3.29). (b) Plots of the numerical solution of $b$ (dashed) at $Pe\,B=20$ and the leading-order asymptotic solution (dotted) given in (3.33).

Figure 7

Figure 8. Plots of the dispersion coefficient as a function of $\alpha$ for $Pe=100$ and $B=0.6$. Circles are results from numerical solutions of the macrotransport equations. Squares are results from BD simulations. The vertical line is given by the equation $\alpha =(1-B)/(1+B)$. The solid line is the asymptotic solution in (3.41).

Figure 8

Figure 9. Plot of the parameter space $(\alpha, B)$. The solid line is given by $1-\alpha = B(1+\alpha )$. In the shaded region, we have $1-\alpha > B(1+\alpha )$.

Figure 9

Figure 10. (a) Plots of the numerical and asymptotic solutions to the average angular drift velocity as a function of $1/\epsilon$ for $B=1,\alpha =0$. (b) Plots of the numerical solutions to the non-dimensional effective long-time dispersion coefficient as a function of $1/\epsilon$ for $B=1,\alpha =0$. The solid line is given by $D^{eff}/D_R = \tilde {C} \epsilon ^{-2/3}$, where $\tilde {C}$ is obtained from numerical data.