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Journal ArticleDOI

Marangoni effects of trace impurities on the motion of long gas bubbles in capillaries

J. Ratulowski, +1 more
- 01 Jan 1990 - 
- Vol. 210, Iss: -1, pp 303-328
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TLDR
In this article, the authors carried out an asymptotic analysis for different convective, diffusive and kinetic timescales and showed that, if transport in the film is mass-transfer limited such that a bulk concentration gradient exists, the film thickness increases by a maximum factor of 4 2/3; over Bretherton's mobile result at low bubble speeds.
Abstract
When a viscous liquid is displaced by a long air bubble in a capillary, it leaves behind a wetting liquid film. A lubrication analysis by Bretherton (1961), which assumes a mobile surface, underpredicts the film thickness at low bubble speeds. In this investigation, the Marangoni effect of small amounts of impurities is shown to be capable of explaining this discrepancy. We carry out an asymptotic analysis for different convective, diffusive and kinetic timescales and show that, if transport in the film is mass-transfer limited such that a bulk concentration gradient exists in the film, the film thickness increases by a maximum factor of 4 2/3; over Bretherton's mobile result at low bubble speeds. Moreover, at large bubble speeds, Bretherton's mobile prediction is approached for all ranges of timescales. For intermediate bubble speeds, the film thickness varies with respect to the bubble speed with an exponent smaller than 2/3 of the mobile theory. These results are favourably compared to literature data on film thickness.

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Citations
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Engineering flows in small devices

TL;DR: An overview of flows in microdevices with focus on electrokinetics, mixing and dispersion, and multiphase flows is provided, highlighting topics important for the description of the fluid dynamics: driving forces, geometry, and the chemical characteristics of surfaces.
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Multiphase monolith reactors: Chemical reaction engineering of segmented flow in microchannels

TL;DR: The use of segmented flow in capillaries, also known as Taylor flow, for reaction engineering purposes has soared in recent years as mentioned in this paper, with an emphasis on the underlying principles.
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Fluid coating on a fiber

TL;DR: In this article, the authors discuss the thickness of the liquid layer entrained by a solid drawn out of a bath, focusing on the case where the solid is a fiber or a wire.
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Inertial and Interfacial Effects on Pressure Drop of Taylor Flow in Capillaries

TL;DR: In this paper, the authors measured the two-phase pressure drop in Taylor slug flow in a capillary and found that if the slug length was smaller than 10 times the capillary diameter, the length-averaged friction factor increased drastically from the single phase value (f = 16/Re) due to differences in curvature at the front and the back of the bubble.
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The pressure drop along rectangular microchannels containing bubbles.

TL;DR: A systematic and quantitative investigation of the influence of surfactants on the flow of fluids in microchannels containing bubbles using an indirect method to derive the pressure in the channel.
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.
Book ChapterDOI

Dragging of a Liquid by a Moving Plate

TL;DR: In this paper, the problem of determining the thickness of the dragged layer as a function of the speed of the motion of the film and of parameters characteristic of the properties of the fluid is investigated.
Journal ArticleDOI

Two-phase displacement in Hele Shaw cells: theory

TL;DR: A theory describing two-phase displacement in the gap between closely spaced planes as a double asymptotic expansion in the small parameters ε and Ca1/3 is developed.
Journal ArticleDOI

Mechanisms of foam flow in porous media: apparent viscosity in smooth capillaries

TL;DR: In this paper, the apparent viscosity of foam flowing through smooth capillaries was measured experimentally and a mathematical model was developed to determine whether the foam exists as bulk foam or as a chain of bubbles where each pair of bubbles is separated by individual lamella, the number of lamellae per unit length of the capillary, and the radius of curvature of the gas-liquid interface.