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The Penetration of a Fluid into a Porous Medium or Hele-Shaw Cell Containing a More Viscous Liquid

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TLDR
In this paper, it was shown that a flow is possible in which equally spaced fingers advance steadily at very slow speeds, such that behind the tips of the advancing fingers the widths of the two columns of fluid are equal.
Abstract
When a viscous fluid filling the voids in a porous medium is driven forwards by the pressure of another driving fluid, the interface between them is liable to be unstable if the driving fluid is the less viscous of the two. This condition occurs in oil fields. To describe the normal modes of small disturbances from a plane interface and their rate of growth, it is necessary to know, or to assume one knows, the conditions which must be satisfied at the interface. The simplest assumption, that the fluids remain completely separated along a definite interface, leads to formulae which are analogous to known expressions developed by scientists working in the oil industry, and also analogous to expressions representing the instability of accelerated interfaces between fluids of different densities. In the latter case the instability develops into round-ended fingers of less dense fluid penetrating into the more dense one. Experiments in which a viscous fluid confined between closely spaced parallel sheets of glass, a Hele-Shaw cell, is driven out by a less viscous one reveal a similar state. The motion in a Hele-Shaw cell is mathematically analogous to two-dimensional flow in a porous medium. Analysis which assumes continuity of pressure through the interface shows that a flow is possible in which equally spaced fingers advance steadily. The ratio λ = (width of finger)/(spacing of fingers) appears as the parameter in a singly infinite set of such motions, all of which appear equally possible. Experiments in which various fluids were forced into a narrow Hele-Shaw cell showed that single fingers can be produced, and that unless the flow is very slow λ = (width of finger)/(width of channel) is close to , so that behind the tips of the advancing fingers the widths of the two columns of fluid are equal. When λ = 1/2 the calculated form of the fingers is very close to that which is registered photographically in the Hele-Shaw cell, but at very slow speeds where the measured value of λ increased from 1/2 to the limit 1.0 as the speed decreased to zero, there were considerable differences. Assuming that these might be due to surface tension, experiments were made in which a fluid of small viscosity, air or water, displaced a much more viscous oil. It is to be expected in that case that λ would be a function of μU/T only, where μ is the viscosity, U the speed of advance and T the interfacial tension. This was verified using air as the less viscous fluid penetrating two oils of viscosities 0.30 and 4.5 poises.

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Citations
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Effects of soil water repellency on infiltration rate and flow instability

TL;DR: In this paper, the effects of soil water-repellency on infiltration rate and the wetting front instability were investigated in a two-dimensional transparent chamber (41.5 cm wide, 50 cm high and 2.8 cm thick) constructed for infiltration experiments using three water repellent Ouddorp sands (The Netherlands) and a wettable silicon sand.
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Experimental study on miscible viscous fingering involving viscosity changes induced by variations in chemical species concentrations due to chemical reactions

TL;DR: In this paper, the authors showed experimentally how a reactive miscible viscous fingering pattern in a radial Hele-Shaw cell changes when the viscosity of the more-viscous liquid is varied owing to variation in chemical species concentration induced by an instantaneous chemical reaction.
Journal ArticleDOI

Phase-field study of three-dimensional steady-state growth shapes in directional solidification

TL;DR: A quantitative phase-field approach is used to study directional solidification in various three-dimensional geometries for realistic parameters of a transparent binary alloy to test existing theories of directional finger growth and interpret the hysteretic nature of the cell-to-dendrite transition.
Journal ArticleDOI

The spreading of surfactant solutions on thin liquid films.

TL;DR: There have been numerous studies which show that Marongoni driven fingering of the spreading surfactant front exists and an attempt has been made to rationalise the results.
Journal ArticleDOI

Dissolution of Dense Chlorinated Solvents into Ground Water: 1. Dissolution from a Well-Defined Residual Source

TL;DR: In this paper, the authors investigated the concentrations and mass removal rates obtainable when simulated ground water is free to flow at least partially around a zone of porous medium that contains solvent in a state of stable, residual saturation.
References
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Journal ArticleDOI

The Instability of Liquid Surfaces when Accelerated in a Direction Perpendicular to their Planes. I

TL;DR: In this article, it was shown that when two superposed fluids of different densities are accelerated in a direction perpendicular to their interface, this surface is stable or unstable according to whether the acceleration is directed from the heavier to the lighter fluid or vice versa.
Journal ArticleDOI

The mechanics of large bubbles rising through extended liquids and through liquids in tubes

TL;DR: In this article, the authors describe measurements of the shape and rate of rise of air bubbles varying in volume from 1·5 to 200 cm. 3 when they rise through nitrobenzene or water.
Journal ArticleDOI

The instability of liquid surfaces when accelerated in a direction perpendicular to their planes. II

TL;DR: In this paper, an apparatus for accelerating small quantities of various liquids vertically downwards at accelerations of the order of 50g ( g being 32.2 ft/sec) is described, and the behavior of small wave-like corrugations initially imposed on the upper liquid surface has been observed by means of high-speed shadow photography.
Journal ArticleDOI

On steady-state bubbles generated by Taylor instability

TL;DR: In this paper, the authors considered the flow of an incompressible heavy liquid past a gas bubble in an infinitely long vertical tube, and the gas in the bubble was considered to be at rest, in a state of constant pressure.
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