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Dynamic simulation of a coated microbubble in an unbounded flow: response to a step change in pressure

Published online by Cambridge University Press:  07 June 2017

M. Vlachomitrou
Affiliation:
Department of Mechanical Engineering, University of Thessaly, Leoforos Athinon, Pedion Areos, 38834 Volos, Greece
N. Pelekasis*
Affiliation:
Department of Mechanical Engineering, University of Thessaly, Leoforos Athinon, Pedion Areos, 38834 Volos, Greece
*
†Email address for correspondence: pel@mie.uth.gr

Abstract

A numerical method is developed to study the dynamic behaviour of an encapsulated bubble when the viscous forces of the surrounding liquid are accounted for. The continuity and Navier–Stokes equations are solved for the liquid, whereas the coating is described as a viscoelastic shell with bending resistance. The Galerkin Finite Element Methodology is employed for the spatial discretization of the flow domain surrounding the bubble, with the standard staggered grid arrangement that uses biquadratic and bilinear Lagrangian basis functions for the velocity and pressure in the liquid, respectively, coupled with a superparametric scheme with $B$ -cubic splines as basis functions pertaining to the location of the interface. The spine method and the elliptic mesh generation technique are used for updating the mesh points in the interior of the flow domain as the shape of the interface evolves with time, with the latter being distinctly superior in capturing severely distorted shapes. The stabilizing effect of the liquid viscosity is demonstrated, as it alters the amplitude of the disturbance for which a bubble deforms and/or collapses. For a step change in the far-field pressure the dynamic evolution of the microbubble is captured until a static equilibrium is achieved. Static shapes that are significantly compressed are captured in the post-buckling regime, leading to symmetric or asymmetric shapes, depending on the relative dilatation to bending stiffness ratio. As the external overpressure increases, shapes corresponding to all the solution families that were captured evolve to exhibit contact as the two poles approach each other. Shell viscosity prevents jet formation by relaxing compressive stresses and bending moments around the indentation generated at the poles due to shell buckling. This behaviour is conjectured to be the inception process leading to static shapes with contact regions.

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Papers
Copyright
© 2017 Cambridge University Press 
Figure 0

Figure 1.Single bubble in an unbounded flow.

Figure 1

Figure 2.(a), (b) Temporal evolution of the shape of a gas bubble. (c) Temporal evolution of the average bubble radius via the breathing mode $\text{P}_{0}$, and the most unstable shape Legendre modes, $\text{P}_{2}$ and $\text{P}_{4}$. The parameters used in the simulation are taken from Tsiglifis & Pelekasis (2007), with $Oh=40$, $S=0.99$ and $\unicode[STIX]{x1D700}_{B}=2$.

Figure 2

Figure 3.(a) Temporal evolution of bubble shape and (b) temporal evolution of breathing mode $\text{P}_{0}$ and shape mode decomposition with the spine method ($Oh=40$, $S=0.7$, $\unicode[STIX]{x1D700}_{B}=2$).

Figure 3

Figure 4.(a) Temporal evolution of bubble shape and (b) temporal evolution of breathing mode $\text{P}_{0}$ and shape mode decomposition with the elliptic mesh generation method ($Oh=40$, $S=0.7$, $\unicode[STIX]{x1D700}_{B}=2$).

Figure 4

Figure 5.Grid obtained for the last snapshot around a gas-filled bubble with the spine method with $100\times 80$ elements ($\unicode[STIX]{x1D707}=5\times 10^{-4}~\text{P}\unicode[STIX]{x1D6FC}~\text{s}$, $\unicode[STIX]{x1D70E}=0.0715~\text{N}~\text{m}^{-1}$, $S=0.7$, $\unicode[STIX]{x1D700}_{B}=2$).

Figure 5

Figure 6.Grid obtained for the last snapshot around a gas-filled bubble with the elliptic mesh generation method with $300\times 160$ elements and a time step $\text{d}t=0.001$ ($\unicode[STIX]{x1D707}=5\times 10^{-4}~\text{P}\unicode[STIX]{x1D6FC}~\text{s}$, $\unicode[STIX]{x1D70E}=0.0715~\text{N}~\text{m}^{-1}$, $S=0.7$, $\unicode[STIX]{x1D700}_{B}=2$).

Figure 6

Figure 7.(a) Temporal evolution of the breathing mode, $\text{P}_{0}$, for a step change disturbance of amplitude $\unicode[STIX]{x1D700}=1$ with the spine and the elliptic mesh method. (b) Time variation of the total energy of the bubble/fluid flow system.

Figure 7

Figure 8.(a) Temporal evolution of bubble shape and (b) temporal evolution of radius and shape mode decomposition for a contrast agent ($R=3.6~\unicode[STIX]{x03BC}\text{m}$, $\unicode[STIX]{x1D707}_{s}=20~\text{Pa}~\text{s}$, $\text{thickness}=1~\text{nm}$, $\unicode[STIX]{x1D712}=0.12~\text{N}~\text{m}^{-1}$, $k_{b}=3\times 10^{-14}~\text{N}~\text{m}$) for a step change disturbance ($\unicode[STIX]{x1D700}=2$) with the spine method. (c) Total energy variation, (d) viscous versus shell damping and (e) distribution among different forms of energy as a function of time.

Figure 8

Figure 9.(a) Temporal evolution of bubble shape and (b) temporal evolution of radius and shape mode decomposition for a contrast agent ($R=3.6~\unicode[STIX]{x03BC}\text{m}$, $\unicode[STIX]{x1D707}_{s}=20~\text{Pa}~\text{s}$, $\text{thickness}=1~\text{nm}$, $\unicode[STIX]{x1D712}=0.12~\text{N}~\text{m}^{-1}$, $k_{b}=3\times 10^{-14}~\text{N}~\text{m}$) for a step change disturbance ($\unicode[STIX]{x1D700}=2$) with the elliptic mesh method. (c) Total energy variation, (d) viscous versus shell damping and (e) distribution among different forms of energy as a function of time.

Figure 9

Figure 10.(a) Temporal evolution of bubble shape and (b) temporal evolution of shape mode decomposition for a contrast agent ($R=3.6~\unicode[STIX]{x03BC}\text{m}$, $\unicode[STIX]{x1D707}_{s}=20~\text{Pa}~\text{s}$, $\text{thickness}=1~\text{nm}$, $\unicode[STIX]{x1D712}=0.12~\text{N}~\text{m}^{-1}$, $k_{b}=3\times 10^{-14}~\text{N}~\text{m}$) for a step change disturbance $(\unicode[STIX]{x1D700}=3)$ with the elliptic mesh method. (c) Grid generated via the elliptic mesh generation technique. (d) Total energy variation and (e) distribution among different forms of energy as a function of time. (f) Time evolution of $\text{P}_{1}$ and (g) time evolution of shape mode decomposition when the origin of the coordinate system is moved.

Figure 10

Figure 11.(a) Temporal evolution of bubble shape and (b) temporal evolution of shape mode decomposition for a contrast agent ($R=3.6~\unicode[STIX]{x03BC}\text{m}$, $\unicode[STIX]{x1D707}_{s}=20~\text{Pa}~\text{s}$, $\text{thickness}=1~\text{nm}$, $\unicode[STIX]{x1D712}=0.12~\text{N}~\text{m}^{-1}$, $k_{b}=3\times 10^{-14}~\text{N}~\text{m}$) for a step change disturbance $(\unicode[STIX]{x1D700}=3.5)$ with the elliptic mesh method. (c) Time evolution of the total shell energy. (d) Temporal evolution of velocity at the two poles. (e) Distribution among different forms of energy and (f) viscous versus shell damping as a function of time.

Figure 11

Figure 12.(a) Temporal evolution of bubble shape and (b) temporal evolution of radius and shape mode decomposition for a contrast agent ($R=3.6~\unicode[STIX]{x03BC}\text{m}$, $\unicode[STIX]{x1D707}_{s}=20~\text{Pa}~\text{s}$, $\text{thickness}=1~\text{nm}$, $\unicode[STIX]{x1D712}=0.24~\text{N}~\text{m}$, $k_{b}=3\times 10^{-14}~\text{N}~\text{m}$) for a step change disturbance ($\unicode[STIX]{x1D700}=2$) with the elliptic mesh method. (c) Time evolution of the total shell energy. (d) Viscous versus shell viscosity and (e) distribution among different forms of energy as a function of time.

Figure 12

Figure 13.(a) Temporal evolution of velocity at the two poles, (b) spatial distribution of shell and viscous stresses at $t=67.5$ and (c) spatial distribution of shell and viscous stresses at $t=107$ for a contrast agent ($R=3.6~\unicode[STIX]{x03BC}\text{m}$, $\unicode[STIX]{x1D707}_{s}=20~\text{Pa}~\text{s}$, $\text{thickness}=1~\text{nm}$, $\unicode[STIX]{x1D712}=0.24~\text{N}~\text{m}$, $k_{b}=3\times 10^{-14}~\text{N}~\text{m}$) for a step change disturbance ($\unicode[STIX]{x1D700}=2$) with the elliptic mesh method.

Figure 13

Figure 14.(a) Time evolution of asymmetric shapes with contact (b) shape modes and (c) radial velocity at the two poles, for the same shell parameters as in figures 12 and 13 and $\unicode[STIX]{x1D700}=3$.

Figure 14

Figure 15.(a) Temporal evolution of bubble shape and (b) temporal evolution of shape mode decomposition for a contrast agent ($R=3.6~\unicode[STIX]{x03BC}\text{m}$, $\unicode[STIX]{x1D707}_{s}=20~\text{Pa}~\text{s}$, $\text{thickness}=1~\text{nm}$, $\unicode[STIX]{x1D712}=0.96~\text{N}~\text{m}^{-1}$, $k_{b}=3\times 10^{-14}~\text{N}~\text{m}$) for a step change disturbance with $\unicode[STIX]{x1D700}=1.3$.

Figure 15

Figure 16.(a) Temporal evolution of bubble shape ($R=3.6~\unicode[STIX]{x03BC}\text{m}$, $\unicode[STIX]{x1D707}_{s}=20~\text{Pa}~\text{s}$, $\text{thickness}=1~\text{nm}$, $\unicode[STIX]{x1D712}=0.96~\text{N}~\text{m}^{-1}$, $k_{b}=3\times 10^{-14}~\text{N}~\text{m}$) for a step change disturbance ($\unicode[STIX]{x1D700}=2$). (b) Time evolution of the radial velocity at the two poles. (c) Total shell energy, (d) distribution among different forms of energy and (e) shell damping as a function of time for $\unicode[STIX]{x1D700}=2$. (f) Spatial distribution of shell and viscous stresses at $t=18.5$.

Figure 16

Figure 17.(a) Final static state and (b) temporal evolution of shape modes, for a step change disturbance with amplitude $\unicode[STIX]{x1D700}=2$ when the viscosity of the surrounding liquid is $\unicode[STIX]{x1D707}_{w}=10^{-5}~\text{Pa}~\text{s}$; $\unicode[STIX]{x1D712}=0.24~\text{N}~\text{m}^{-1}$.

Figure 17

Figure 18.(a) Temporal evolution of bubble shape and (b) temporal evolution of radius and shape mode decomposition for a contrast agent ($R=3.6~\unicode[STIX]{x03BC}\text{m}$, $\unicode[STIX]{x1D707}_{s}=0$, $\text{thickness}=1~\text{nm}$, $\unicode[STIX]{x1D712}=0.24~\text{N}~\text{m}^{-1}$, $k_{b}=3\times 10^{-14}~\text{N}~\text{m}$) for a step change disturbance ($\unicode[STIX]{x1D700}=2$) with the elliptic mesh method. (c) Radial velocity and (d) distribution of the shell energy among its different forms.

Figure 18

Figure 19.Schematic representation of the physical and the computational domain for the case of a bubble in an unbounded flow.