Hostname: page-component-7b7567c8c-2n9c9 Total loading time: 0 Render date: 2026-11-15T11:54:29.480Z Has data issue: false hasContentIssue false

Impact of polydispersity and confinement on diffusion in hydrodynamically interacting colloidal suspensions

Published online by Cambridge University Press:  01 September 2021

Emma Gonzalez
Affiliation:
Department of Chemical Engineering, Stanford University, Stanford, CA 94305, USA
Christian Aponte-Rivera
Affiliation:
Department of Chemical Engineering, Cornell University, Ithaca, NY 14850, USA
Roseanna N. Zia*
Affiliation:
Department of Chemical Engineering, Stanford University, Stanford, CA 94305, USA
*
†Email address for correspondence: rzia@stanford.edu

Abstract

We present a computational study of the equilibrium dynamics of a polydisperse hard-sphere colloidal dispersion confined in a spherical cavity. We account for many-body hydrodynamic and lubrication interactions between particles and with the confining cavity utilizing our confined Stokesian dynamics model, expanded here for size polydispersity. We find that, even though the tendency of polydispersity to homogenize structure in a suspension is still present in confinement, strong correlations induced by the cavity resist homogenization. Although seemingly opposite, these two effects have a common driver, which is to maximize configurational entropy of particles in the cavity interior. These structural effects couple with the hydrodynamics to change the particle dynamics: polydispersity weakens lubrication effects near the cavity wall, allowing small (large) particles to diffuse faster (slower) than in a monodisperse suspension. As a small (large) particle gets farther from the wall, polydispersity weakens many-body hydrodynamic couplings, driving diffusivity up (down). While the local cage dynamics dominates short-time self-diffusion, long-time dynamics is also affected. In the concentrated regime, polydispersity and confinement combine to induce radial de-mixing into size-segregated populations. The cavity becomes the most influential ‘nearest neighbour’, setting the length scale of and dynamics within these radial domains. This intermediate length-scale caging makes the angular dynamics insensitive to polydispersity but leads to radial long-time mean-square displacement that changes qualitatively with volume composition. These results hold promise for explaining colloidal-scale physics implicated in the functioning of biological cells, and the engineering of non-living confined colloids where size de-mixing could be useful in the design of encapsulated micro-reactors and therapeutic vesicles.

Information

Type
JFM Papers
Copyright
© The Author(s), 2021. Published by Cambridge University Press
Figure 0

Figure 1.(a) Conceptual sketch of model system for a spherically confined bidisperse ($K=2$) suspension with (b) particle labelling based on size.

Figure 1

Figure 2.Conceptual sketch of binning scheme. The spherical cavity volume is radially divided into 100 bins of constant width $\Delta y$ (thus, each of varying volume). The bins span the entire cavity, from centre to just inside the cavity wall, with the centre of the bin, $y_m$, defining its location. The final (in this case, 100th) bin is located at the closest permissible position of the centre of the smallest particle relative to the cavity wall.

Figure 2

Figure 3.Cavity-centred radial distribution function $g(y)$ for monodisperse and bidisperse suspensions confined in a spherical cavity. Particle-size ratio is $\lambda _{p_2} = 2$, total volume fraction is $\phi =0.40$ and the size of large particles relative to the cavity is $\lambda _{c_2} = 0.2$. Several volume compositions are shown, plotted in terms of the volume fraction of large particles relative to the total volume fraction, $0.0 \leq \phi _2/\phi \leq 1.0$.

Figure 3

Figure 4.Confinement preserves correlations, even with pronounced polydispersity. The cavity-centred radial distribution function of colloidal spheres inside a cavity (symbols) computed in the present study via dynamic simulation is shown alongside the pair distribution function of the same size particles in an unconfined suspension (curves) obtained from the Percus–Yevick closure relation (Smith et al.2008), at the same volume compositions. All are plotted as a function of the separation between hard-sphere surfaces, i.e. particle-to-cavity (confined data) and particle-to-particle surface separation (unconfined data). Total volume fraction is $\phi =0.40$, particle-size ratio is $\lambda _{p_2} = 2$; for the confined data, the cavity size is specified based on the large particle-to-cavity size ratio $\lambda _{c_2} = 0.2$. (a) Correlations between small particles as large particles become more numerous in the suspension. Three volume compositions $\phi _1/\phi$ are shown. (b) Correlations between large particles as small particles become more numerous in the suspension. Three volume compositions $\phi _2/\phi$ are shown.

Figure 4

Figure 5.The radial component of the short-time self-diffusivity obtained here utilizing our new confined mobility functions (see supplementary material, equation (S3)), implemented in polydisperse confined Stokesian dynamics simulations. Plotted as a function of the normalized particle positions in the cavity, for volume compositions of the large particles (symbols) $0.0 \leq \phi _2/\phi \leq 1.0$ with particle-size ratio $\lambda _{p_2} = 2$, volume fraction $\phi =0.10$ and large particle-to-cavity relative size $\lambda _{c_2} = 0.2$. Dashed lines are the proposed ‘colloidal Dalton's law’ where a simple number average of the two monodisperse curves is used to predict the bidisperse $D_{0}^{s_\parallel }/D_{0,1}$.

Figure 5

Figure 6.The radial component of the short-time self-diffusivity obtained here utilizing polydisperse confined Stokesian dynamics simulations, plotted as a function of the normalized particle positions in the cavity. Volume compositions of the large particles are $0.0 \leq \phi _2/\phi \leq 1.0$; particle-size ratio is $\lambda _{p_2} = 2$, total volume fraction is $\phi =0.40$ and large particle-to-cavity size ratio is $\lambda _{c_2} = 0.2$. Transverse short-time self-diffusivity data can be found in Appendix B, figure 18.

Figure 6

Figure 7.Species-specific contributions to the radial component of the short-time self-diffusivity, plotted as a function of distance from the cavity centre, for the same conditions as figure 6. (a) Diffusivity of small particles in a suspension at fixed total volume fraction $\phi =0.40$, as large particles become more numerous. (b) Diffusivity of large particles in a suspension at fixed total volume fraction $\phi =0.40$, as small particles become more numerous.

Figure 7

Figure 8.The MSD $\langle r^{2}_{\parallel } \rangle /a_1^{2}$ as a function of time at moderate volume fraction ($\phi =0.25$) for particle-size ratio $\lambda _{p_2} = 4/3$ and confinement $\lambda _{c_2} = 0.2$. Volume composition $\phi _2/\phi$ varies from one monodisperse limit to the other as shown in legend. (a) The MSD is averaged over all particles, giving a measure of how polydispersity affects the entire suspension-averaged dynamics. The average dynamics of (a) small and (b) large particles in a surrounding suspension, as they change in the presence of more (a) large or (b) small particles, at fixed total volume fraction. (a) Averaged over all particles. (b) Small-particle contribution. (c) Large-particle contribution.

Figure 8

Figure 9.The MSD $\langle r^{2}_{\parallel } \rangle /a_1^{2}$ for (a) monodisperse and bidisperse suspensions at total volume fraction $\phi =0.40$, with particle size ratio $\lambda _{p_2} = 4/3$, confinement $\lambda _{c_2} = 0.2$, for several volume compositions of large particles $\phi _2/\phi$. The MSD of either (b) small $\langle r^{2}_{\parallel } \rangle _1/a_1^{2}$ or (c) large $\langle r^{2}_{\parallel } \rangle _2/a_1^{2}$ particles at the same suspension compositions. (a) Averaged over all particles. (b) Small-particle contribution. (c) Large-particle contribution.

Figure 9

Figure 10.The MSD $\langle r^{2}_{\perp } \rangle /a_1^{2}$ for (a) monodisperse and bidisperse suspensions at total volume fraction $\phi =0.40$, particle-size ratio $\lambda _{p_2} = 4/3$ and confinement $\lambda _{c_2} = 0.2$, for several volume compositions of large particles $\phi _2/\phi$. The MSD of either (b) small $\langle r^{2}_{\perp } \rangle _1/a_1^{2}$ or (c) large $\langle r^{2}_{\perp } \rangle _2/a_1^{2}$ particles at the same suspension compositions. (a) Averaged over all particles. (b) Small-particle contribution. (c) Large-particle contribution.

Figure 10

Figure 11.Confinement-induced layering convolves with polydispersity to induce de-mixing into size-segregated radial layers that change with volume composition. Contour plots of the average distribution of particle types, calculated by monitoring the occupants in each of the radial bins as particles diffuse over a time $1200 \ a^{2}_1/D_{0,1}$, the average time required for particles to explore the length of the cavity. Occupants were identified only based on size, with a value 1 assigned to small particles and a value 2 assigned to large particles. Seven plots are shown, corresponding to different volume compositions. Colour scheme shown in legend.

Figure 11

Figure 12.(a) Per cent increment in the total number of particles at wall contact with respect to a monodisperse (all-large) suspension, $100\,\%\times [(N_{tot}-N_{{mono, 2}})/N_{{mono, 2}}]_{{wall}}$, as it changes with bidispersity. (b) Fraction of large (left axis) and small (right axis) particles at wall contact.

Figure 12

Figure 13.Cavity-centred RDF $g(y)$ for monodisperse and bidisperse suspensions confined in a spherical cavity. The total volume fraction is $\phi =0.40$, the particle size ratio $\lambda _{p_2}$ and the size of large particles relative to the cavity are $\lambda _{c_2}$ for (a) $\lambda _{p_2}=2.0$ and $\lambda _{c_2}=0.15$ and (b) $\lambda _{p_2}=4/3$ and $\lambda _{c_2}=0.2$. Several volume compositions are shown, plotted in terms of the volume fraction of large particles relative to the total volume fraction, $0.0 \leq \phi _2/\phi \leq 1.0$.

Figure 13

Figure 14.Cavity-centred RDF $g(y)$ for (a) large and (b) small particles in monodisperse and bidisperse suspensions confined in a spherical cavity. Particle-size ratio is $\lambda_{p_2}=2$, total volume fraction is $\phi =0.40$. The size of large particles relative to the cavity is $\lambda_{c_2} = 0.2$ and that of the small particles is $\lambda_{c_1} = 0.1$. Several volume compositions are shown, plotted in terms of the volume fraction of large particles relative to the total volume fraction, $0.0 \leq \phi_2/\phi \leq 1.0.$

Figure 14

Figure 15.Cavity-centred RDF $g(y)$ for monodisperse and bidisperse suspensions confined in a spherical cavity for two total volume fractions (a) $\phi =0.25$ and (b) $\phi =0.10$. The particle-size ratio is $\lambda _{p_2} = 2$ and the size of large particles relative to the cavity is $\lambda _{c_2} = 0.2$. Several volume compositions are shown, plotted in terms of the volume fraction of large particles relative to the total volume fraction, $0.0 \leq \phi _2/\phi \leq 1.0$.

Figure 15

Figure 16.The perpendicular component of the short-time self-diffusivity $D^{s\perp }_{0}/D_{0,1}$ plotted as a function of the normalized particle position in the cavity, for several values of volume composition of large particles (symbols) $0.0 \leq \phi _2/\phi \leq 1.0$ with particle size ratio $\lambda _{p_2} = 2$, volume fraction $\phi =0.10$ and large particle-to-cavity relative size $\lambda _{c_2} = 0.2$. Dashed lines are the proposed ‘colloidal Dalton's law’ where a simple number average of the two monodisperse curves is used to predict of the bidisperse $D_{0}^{s_\perp }/D_{0,1}$.

Figure 16

Figure 17.The radial component of the short-time self-diffusivity averaged over (a) only large and (b) only small particles and plotted as a function of the normalized particle positions in the cavity, for volume compositions of the large particles $0.0 \leq \phi _2/\phi \leq 1.0$ with particle-size ratio $\lambda _{p_2} = 2$, volume fraction $\phi =0.10$ and large particle-to-cavity relative size $\lambda _{c_2} = 0.2$.

Figure 17

Figure 18.The perpendicular component of the short-time self-diffusivity obtained here utilizing polydisperse confined Stokesian dynamics simulations, plotted as a function of the normalized particle positions in the cavity. Volume compositions of the large particles are $0.0 \leq \phi _2/\phi \leq 1.0$; particle-size ratio is $\lambda _{p_2} = 2$, total volume fraction is $\phi =0.40$ and large particle-to-cavity size ratio is $\lambda _{c_2} = 0.2$.

Figure 18

Figure 19.Comparison of structure for large particles in monodisperse, $\phi _{2}/\phi = 100\,\%$, and bidisperse suspensions, $\phi _{2}/\phi = 95\,\%$, with particle-size ratio $\lambda _{p_2} = 2$, volume fraction $\phi =0.40$ and large particle-to-cavity relative size $\lambda _{c_2} = 0.2$.

Figure 19

Figure 20.The STSD coefficient (filled symbols) and STSD coefficient considering only the many-body (far-field) coupling contribution (open symbols) for (a) small and (b) large particles in confined suspensions $\lambda _{c2} = 0.2$ at a volume fraction $\phi =0.4$, particle-size ratio $\lambda _{p2} = 2.0$ and for several volume compositions $0\,\%\le \phi _2/\phi \le 100\,\%$.

Figure 20

Figure 21.Cavity-centred RDF g(y) for monodisperse and bidisperse suspensions confined in a spherical cavity (a) averaged over all the particles and (b) averaged over either small or large particles. Particle-size ratio is $\lambda_{p_2} = 4/3$, total volume fraction is $\phi=0.40$ and the size of large particles relative to the cavity is $\lambda_{c_2} = 0.2$. Several volume compositions are shown, plotted in terms of the volume fraction of large particles relative to the total volume fraction, $0.0 \leq \phi_2/\phi \leq 1.0$.

Supplementary material: File

Gonzalez et al. supplementary material

Gonzalez et al. supplementary material

Download Gonzalez et al. supplementary material(File)
File 643.5 KB