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Journal ArticleDOI

The motion of long bubbles through viscoelastic fluids in capillary tubes

Vishal Gauri, +1 more
- 05 Nov 1999 - 
- Vol. 38, Iss: 5, pp 458-470
TLDR
In this paper, the authors investigated the influence of viscoelastic material properties on the hydrodynamic coating thickness and local flow kinematics of a gas bubble penetration in a capillary tube and found that the coating thickness in this process increases with an increase in the extensionally thickening nature of the fluid.
Abstract
The penetration of long gas bubble through a viscoelastic fluid in a capillary tube has been studied in order to investigate the influence of viscoelastic material properties on the hydrodynamic coating thickness and local flow kinematics. Experiments are conducted for three tailored ideal elastic (Boger) fluids, designed to exhibit similar steady shear properties but substantially different elastic material functions. This allows for the isolation of elastic and extensional material effects on the bubble penetration process. The shear and extensional rheology of the fluid is characterized using rotational and filament stretching rheometers (FSR). The fluids are designed such that the steady-state extensional viscosity measured by the FSR at a Deborah number (De) greater than 1 differs over three orders of magnitude (Trouton ratio = 103–106). The experiment set up to measure the hydrodynamic coating thickness is designed to provide accurate data over a wide range of capillary numbers (0.01 < Ca < 100). The results indicate that the coating thickness in this process increases with an increase in the extensionally thickening nature of the fluid. Experiments are also conducted using several different capillary tube diameters (0.1 < D < 1 cm), in order to compare responses at similar Ca but different flow De. Suitable scaling methods and nonlinear viscoelastic constitutive equations are explored to characterize the displacement process for polymeric fluids. Bubble tip shapes at different De are recorded using a CCD camera, and measured using an edge detection algorithm. The influence of the mixed flow field on the bubble tip shape is examined. Particle tracking velocimetry experiments are conducted to compare the influence of viscoelastic properties on the velocity field in the vicinity of the bubble tip. Local shear and extension rates are calculated in the vicinity of the bubble tip from the velocity data. The results provide quantitative information on the influence of elastic and extensional properties on the bubble penetration process in gas-assisted injection molding. The bubble shape and velocity field information provides a basis for evaluating the performance of constitutive equations in mixed flow.

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Citations
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Journal ArticleDOI

A numerical study of the motion of a spherical drop rising in shear-thinning fluid systems

TL;DR: In this paper, the authors considered the dynamical processes of a Newtonian spherical drop rising freely through shear-thinning fluids expressed by the generalized Cross-Carreau (Carreaux-Yasuda) model.
Journal ArticleDOI

A model for film-forming with Newtonian and shear-thinning fluids

TL;DR: In this paper, the formation of a thin film by the slow penetration of a gas bubble into a liquid filled tube, and the withdrawal of a planar substrate from a liquid-filled gap, is investigated theoretically for the cases of both Newtonian and shear-thinning liquids; the latter conforming to either a power-law or Ellis model.
Journal ArticleDOI

Primary and secondary gas penetration during gas-assisted injection molding. Part I: Formulation and modeling

TL;DR: In this article, a theoretical study on the transient gas-liquid interface development and gas penetration behavior during the cavity filling and gas packing stage in the gas-assisted injection molding (GAIM) of a tube cavity is carried out.
Journal ArticleDOI

Modelling and simulation of moving interfaces in gas-assisted injection moulding process

TL;DR: In this paper, the authors introduced the mathematical models of gas-liquid two-phase flow, in which the multi-mode eXtended Pom-Pom (XPP) model was selected to predict the viscoelastic behavior of polymer melt.
Journal ArticleDOI

Yield-stress fluid deposition in circular channels

TL;DR: In this article, the authors used scaling arguments to extend the analytical expression of Bretherton's law to YSFs in circular tubes and showed that the thickness of the film deposited behind a long bubble invading a Newtonian fluid is known to increase with the capillary number power.
References
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Journal ArticleDOI

The motion of long bubbles in tubes

TL;DR: In this article, the authors provided a partial theory of the indicator bubble commonly used to measure liquid flowrates in capillaries, and showed that the bubble will not rise at all if where ρ is the difference in density between the fluids inside and outside the bubble.
Journal ArticleDOI

Deposition of a viscous fluid on the wall of a tube

TL;DR: In this article, the amount of fluid left behind when a viscous liquid is blown from an open-ended tube is measured, and the results show that it is not negligible.
Journal ArticleDOI

A filament stretching device for measurement of extensional viscosity

V. Tirtaatmadja, +1 more
- 01 Nov 1993 - 
TL;DR: In this paper, a filament stretching device for measuring the extensional viscosity of low-viscosity liquids is presented, where the fluid sample is held between two disks which move apart at an increasing velocity so that the extension rate, based on the filament midpoint diameter, is constant.
Journal ArticleDOI

Flow patterns in liquid slugs during bubble-train flow inside capillaries

TL;DR: In this paper, high-speed video imaging was used to characterize liquid flow patterns and velocity distributions inside liquid slugs were determined by particle imaging velocimetry (PIV).
Journal ArticleDOI

On the motion of bubbles in capillary tubes

TL;DR: The average thickness of the wetting film left behind during the slow passage of an air bubble in a water-filled capillary tube of circular cross-section has been determined experimentally as a function of bubble speed and bubble length as mentioned in this paper.