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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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Fingering versus stability in the limit of zero interfacial tension

TL;DR: This work investigates the non-linear growth that occurs after the instability has been fully established and finds a rich variety of patterns that are characterized by the viscosity ratio between the inner and the outer fluid, η(in)/η(out), as distinct from the most-unstable wavelength, which determines the onset of the instability.
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Instability, self-organization and pattern formation in thin soft films.

TL;DR: This article classify the instability of a thin polymer film into three broad categories, which are: instability of an ultra-thin (<100 nm) viscous film engendered by amplification of thermally excited surface capillary waves due to interfacial dispersive van der Waals forces, and instability arising from the attractive inter-surface interactions.
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Immiscible displacement in a channel: simulations of fingering in two dimensions

TL;DR: In this article, the authors used a lattice Boltzmann multiphase/multicomponent model to study the flow of two immiscible fluids with different viscosities.
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Cohesive failure of thin layers of soft model adhesives under tension

TL;DR: In this paper, the authors derived a theoretical expression for the force-distance curve as a function of the yield stress, which describes the experimental results very well and confirmed the morphology of the fingering instabilities.
Journal ArticleDOI

On the generation of instabilities in variable density flow

TL;DR: In this article, the authors used a variable density flow and transport code to study how the style of interfacial perturbation controls the pattern of instability development and showed that numerical errors in a mass transport code can serve as a perturbing function and lead to the development of instabilities.
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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