Javascript must be enabled to continue!
Spatiotemporal Viscosity Gradients Shape Breakup and Relaxation in Non-Newtonian Drops
View through CrossRef
Unlike elongated Newtonian drops, whose relaxation to a sphere is approximately exponential and governed by a single characteristic timescale, particle-filled drops can exhibit complex, multistage relaxation and may fail to recover a spherical shape. These dynamical features are important because they determine the morphology of particle-filled immiscible blends, which in turn controls their macroscopic properties. Our prior experiments demonstrated that, at sufficiently high particle loading, the initially rapid relaxation eventually slows down and appears to arrest at a finite, non-spherical deformation. However, the experiments could not resolve the spatiotemporal evolution of internal quantities such as viscosity, velocity gradients, and stress fields. Here, we investigate whether the retardation and subsequent apparent arrest of initially elongated drops can arise solely from strong shear thinning, without invoking fluid elasticity or a true yield stress. Motivated by experiments on particle-filled polyisobutylene drops, we perform axisymmetric, two-phase volume-of-fluid simulations in which the drop phase follows a Carreau–Yasuda constitutive law and the suspending fluid is Newtonian. The numerical method is first validated against classical predictions for Newtonian drop relaxation. We find that Carreau–Yasuda drops exhibit a two-stage response comprising rapid initial relaxation followed by pronounced late-time retardation. The onset, magnitude and rate of this slowing are governed by a dimensionless parameter S that compares the material shear-thinning rate scale with the characteristic capillary relaxation rate. Spatially resolved fields reveal that geometrically induced low-strain-rate regions near the retracting poles enter the high-viscosity regime before the remainder of the drop. These localized regions resist the flow required for continued shape recovery and act as viscous anchors, producing a self-reinforcing positive coupling between decreasing strain rate, increasing viscosity, and suppressed relaxation. Because the Carreau–Yasuda fluid never becomes truly unyielded, we introduce an operational stress-based criterion for apparent arrest using the characteristic stress η0/λ where η0 is the zero-shear viscosity of the Carreau–Yasuda fluid, and λ is the Carreau–Yasuda relaxation time. We demonstrate and rationalize via a stress balance argument that the deformation at apparent-arrest Darr ∝ S in this weak-to-moderate deformation regime. Taken together, spatiotemporal variations in the viscosity, strain-rate, and normalized-stress fields identify the microscopic origin of the arrested relaxation observed experimentally: a geometrically inherited low-strain-rate region near the drop ends, amplified by the shear-thinning constitutive response into a high-viscosity anchor, which couples back through positive feedback and stabilizes the drop at a finite arrested deformation.
American Chemical Society (ACS)
Title: Spatiotemporal Viscosity Gradients Shape Breakup and Relaxation in Non-Newtonian Drops
Description:
Unlike elongated Newtonian drops, whose relaxation to a sphere is approximately exponential and governed by a single characteristic timescale, particle-filled drops can exhibit complex, multistage relaxation and may fail to recover a spherical shape.
These dynamical features are important because they determine the morphology of particle-filled immiscible blends, which in turn controls their macroscopic properties.
Our prior experiments demonstrated that, at sufficiently high particle loading, the initially rapid relaxation eventually slows down and appears to arrest at a finite, non-spherical deformation.
However, the experiments could not resolve the spatiotemporal evolution of internal quantities such as viscosity, velocity gradients, and stress fields.
Here, we investigate whether the retardation and subsequent apparent arrest of initially elongated drops can arise solely from strong shear thinning, without invoking fluid elasticity or a true yield stress.
Motivated by experiments on particle-filled polyisobutylene drops, we perform axisymmetric, two-phase volume-of-fluid simulations in which the drop phase follows a Carreau–Yasuda constitutive law and the suspending fluid is Newtonian.
The numerical method is first validated against classical predictions for Newtonian drop relaxation.
We find that Carreau–Yasuda drops exhibit a two-stage response comprising rapid initial relaxation followed by pronounced late-time retardation.
The onset, magnitude and rate of this slowing are governed by a dimensionless parameter S that compares the material shear-thinning rate scale with the characteristic capillary relaxation rate.
Spatially resolved fields reveal that geometrically induced low-strain-rate regions near the retracting poles enter the high-viscosity regime before the remainder of the drop.
These localized regions resist the flow required for continued shape recovery and act as viscous anchors, producing a self-reinforcing positive coupling between decreasing strain rate, increasing viscosity, and suppressed relaxation.
Because the Carreau–Yasuda fluid never becomes truly unyielded, we introduce an operational stress-based criterion for apparent arrest using the characteristic stress η0/λ where η0 is the zero-shear viscosity of the Carreau–Yasuda fluid, and λ is the Carreau–Yasuda relaxation time.
We demonstrate and rationalize via a stress balance argument that the deformation at apparent-arrest Darr ∝ S in this weak-to-moderate deformation regime.
Taken together, spatiotemporal variations in the viscosity, strain-rate, and normalized-stress fields identify the microscopic origin of the arrested relaxation observed experimentally: a geometrically inherited low-strain-rate region near the drop ends, amplified by the shear-thinning constitutive response into a high-viscosity anchor, which couples back through positive feedback and stabilizes the drop at a finite arrested deformation.
Related Results
Experimental study on drop breakup time and breakup rate with drop swarm in a stirred tank
Experimental study on drop breakup time and breakup rate with drop swarm in a stirred tank
Drop breakup experiments were carried out in a stirred tank using the
high-speed online camera. Breakup behaviors of drop breakup time,
multiple breakage, and breakup rate were inv...
Localized Breakup Instabilities for a Liquid Jet in Crossflow
Localized Breakup Instabilities for a Liquid Jet in Crossflow
Abstract
Liquid fuel jet in Crossflow (LJIC) is significant to the aviation industry since it is a vital technique for atomization. The hydrodynamic instability mech...
New Compositional Models for Calculating Viscosity of Crude Oils
New Compositional Models for Calculating Viscosity of Crude Oils
Abstract
Crude oil viscosity is an important physical property that controls and influences the flow of oil through porous media and pipelines. Hence, it is the b...
Bubble breakup dynamics in a semicircular pore throat microchannel
Bubble breakup dynamics in a semicircular pore throat microchannel
This work investigates the dynamics of gas–liquid interface breakup and bubble formation in oil microchannels (with oil as the continuous phase). A high-speed camera was utilized t...
<b>Regional Tear Film Instability in Dry Eye Disease: A Comparative Analysis of Central and Inferior Tear Breakup Time</b>
<b>Regional Tear Film Instability in Dry Eye Disease: A Comparative Analysis of Central and Inferior Tear Breakup Time</b>
Background: Dry eye disease is a multifactorial ocular surface disorder characterized by tear film instability, ocular discomfort, and visual disturbance. Conventional tear breakup...
Vortical structures and primary breakup of liquid metal in gas atomization
Vortical structures and primary breakup of liquid metal in gas atomization
High-pressure gas atomization (HPGA) is a widely used method for producing metal powders using high-velocity gas jets, offering high efficiency for large-scale production. Achievin...
THE PROBLEMS OF HYDRODYNAMIC NON-ISOTHERMAL LUBRICATION
THE PROBLEMS OF HYDRODYNAMIC NON-ISOTHERMAL LUBRICATION
The classical hydrodynamic theory of slide bearing lubrication has been constituted on the assumption of constant pressure and viscosity perpendicular to the thin oil layer thickne...
Feedbacks between a non-Newtonian upper mantle, mantle viscosity structure and mantle dynamics
Feedbacks between a non-Newtonian upper mantle, mantle viscosity structure and mantle dynamics
SUMMARY
Previous studies have shown that a low viscosity upper mantle can impact the wavelength of mantle flow and the balance of plate driving to resisting force...

