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Evolution and stationarity of liquid toroidal drop in compressional Stokes flow

Published online by Cambridge University Press:  27 November 2017

B. K. Ee
Affiliation:
Department of Chemical Engineering, Technion-Israel Institute of Technology, Haifa 3200003, Israel
O. M. Lavrenteva
Affiliation:
Department of Chemical Engineering, Technion-Israel Institute of Technology, Haifa 3200003, Israel
I. Smagin
Affiliation:
Department of Chemical Engineering, Technion-Israel Institute of Technology, Haifa 3200003, Israel
A. Nir*
Affiliation:
Department of Chemical Engineering, Technion-Israel Institute of Technology, Haifa 3200003, Israel
*
†Email address for correspondence: avinir@tx.technion.ac.il

Abstract

Dynamics of fluid tori in slow viscous flow is studied. Such tori are of interest as future carriers of biological and medicinal substances and are also viewed as potential building blocks towards more complex particles. In this study the immiscible ambient fluid is subject to a compressional flow (i.e., bi-extensional flow), and it comprises a generalization of our earlier report on the particular case with viscosity ratio $\unicode[STIX]{x1D706}=1$ (see Zabarankin et al., J. Fluid Mech., vol. 785, 2015, pp. 372–400), where $\unicode[STIX]{x1D706}$ is the ratio between the torus viscosity and that of the ambient fluid. It is found that, for all viscosity ratios, the torus either collapses towards the axis of symmetry or expands indefinitely, depending on the initial conditions and the capillary number, Ca. During these dynamic patterns the cross-sections exhibit various forms of deformation. The collapse and expansion dynamic modes are separated by a limited deformation into a deformed stationary state which appears to exist in a finite interval of the capillary number, $0<Ca<Ca_{cr}(\unicode[STIX]{x1D706})$ , and is unstable to axisymmetric disturbances, which eventually cause the torus either to collapse or to expand indefinitely. The characteristic dimensions and shapes of these unstable stationary tori and their dependence on the physical parameters Ca and $\unicode[STIX]{x1D706}$ are reported.

Information

Type
JFM Papers
Copyright
© 2017 Cambridge University Press 
Figure 0

Figure 1. An axisymmetric toroidal drop.

Figure 1

Figure 2. The dynamic collapse of an axisymmetric toroidal drop in the absence of external flow. Experimental data (diamonds) are quoted from Pairam & Fernández-Nieves (2009). Solid and dotted curves obtained numerically in this work with $\unicode[STIX]{x1D706}=0.01$, denote deformation with $R_{min}$ calculated at $|z|\geqslant 0$ and $z=0$, respectively. Dashed–dotted and dashed curves were reported by Zabarankin et al. (2015) for the above-mentioned calculation of $R_{min}$.

Figure 2

Figure 3. Dynamic deformation of toroidal drop, initially with circular cross-section. $Ca=0.08$. (a) $\unicode[STIX]{x1D706}=0.1$, $R=1.1$; (b) $\unicode[STIX]{x1D706}=0.1$, $R=1.4$; (c) $\unicode[STIX]{x1D706}=10,R=1.1$; (d) $\unicode[STIX]{x1D706}=10$, $R=1.4$. The origin of the abscissa coincides with the axis of symmetry.

Figure 3

Figure 4. Evolution of $R_{max}$ (a) and $R_{min}$ (b) in the process of indefinite expansion for various values of the viscosity ratio. $Ca=0.08$, initial radius $R=1.4$.

Figure 4

Figure 5. Evolution of the Taylor deformation parameters in the process of indefinite expansion for various values of the viscosity ratio. $Ca=0.08$, $R=1.4$. (a) Toroidal deformation parameter. (b) Cross-section deformation parameter.

Figure 5

Figure 6. Dynamic deformation of toroidal drop, initially with circular cross-section at relatively high capillary number $Ca=0.5$. (a) $\unicode[STIX]{x1D706}=0.1$, $R=0.64$; (b) $\unicode[STIX]{x1D706}=0.1$, $R=0.68$; (c) $\unicode[STIX]{x1D706}=10$, $R=0.64$; (d) $\unicode[STIX]{x1D706}=10$, $R=0.68$. The origin of the abscissa coincides with the axis of symmetry.

Figure 6

Table 1. Critical initial radius of the torus.

Figure 7

Figure 7. Evolution of $R,R_{min}$ and cross-section deformation parameter $D_{1}$ to a stationary torus, initially with circular cross-section and $R\sim R_{c},Ca=0.15$, $\unicode[STIX]{x1D706}=10$.

Figure 8

Figure 8. The dependence of $R_{c}$ on the capillary number (a) and on the viscosity ratio (b). $Ca for all $\unicode[STIX]{x1D706}$.

Figure 9

Figure 9. Taylor deformation factor of unstable stationary state toroidal drops. $0.

Figure 10

Figure 10. Cross-section shapes of unstable stationary tori. (a) Near-circular cross-sections, $Ca=0.04$. (b) Oval cross-section, $Ca=0.14$. (c) Highly deformed cross-section at near-critical Ca, $D\sim 0.72$. The origin of the abscissa coincides with the axis of symmetry.

Figure 11

Figure 11. Tangential velocity component on the interface of deformed tori at near-critical Ca. The origin of the abscissa coincides with the axis of symmetry.

Figure 12

Figure 12. Streamlines patterns of unsteady stationary tori at intermediate and high (near collapse) capillary numbers. (a) $\unicode[STIX]{x1D706}=0.1$, $Ca=0.14$; (b) $\unicode[STIX]{x1D706}=0.1$, $Ca=0.245$; (c) $\unicode[STIX]{x1D706}=10$, $Ca=0.14$; (d) $\unicode[STIX]{x1D706}=10$, $Ca=0.172$.

Figure 13

Figure 13. A comparison of stationary tori with deformed cross-section with ‘stationary’ tori having circular cross-section (dots, Zabarankin 2016). $R_{c}$, solid lines, $R$, dashed lines.

Figure 14

Figure 14. Critical capillary number as a function of the viscosity ratio.