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. 2012 Dec 11;109(50):20309-13.
doi: 10.1073/pnas.1219009109. Epub 2012 Nov 27.

A mathematical model of fluid and gas flow in nanoporous media

Affiliations

A mathematical model of fluid and gas flow in nanoporous media

Paulo J M Monteiro et al. Proc Natl Acad Sci U S A. .

Abstract

The mathematical modeling of the flow in nanoporous rocks (e.g., shales) becomes an important new branch of subterranean fluid mechanics. The classic approach that was successfully used in the construction of the technology to develop oil and gas deposits in the United States, Canada, and the Union of Soviet Socialist Republics becomes insufficient for deposits in shales. In the present article a mathematical model of the flow in nanoporous rocks is proposed. The model assumes the rock consists of two components: (i) a matrix, which is more or less an ordinary porous or fissurized-porous medium, and (ii) specific organic inclusions composed of kerogen. These inclusions may have substantial porosity but, due to the nanoscale of pores, tubes, and channels, have extremely low permeability on the order of a nanodarcy (~109-²¹ m² ) or less. These inclusions contain the majority of fluid: oil and gas. Our model is based on the hypothesis that the permeability of the inclusions substantially depends on the pressure gradient. At the beginning of the development of the deposit, boundary layers are formed at the boundaries of the low-permeable inclusions, where the permeability is strongly increased and intensive flow from inclusions to the matrix occurs. The resulting formulae for the production rate of the deposit are presented in explicit form. The formulae demonstrate that the production rate of deposits decays with time following a power law whose exponent lies between -1/2 and -1. Processing of experimental data obtained from various oil and gas deposits in shales demonstrated an instructive agreement with the prediction of the model.

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Conflict of interest statement

The authors declare no conflict of interest.

Figures

Fig. 1.
Fig. 1.
Schematic shows a small region within a shale, consisting of (I) a porous, fissurized matrix that has a permeability sufficient to be treated by classic subterranean fluid mechanics and (II) a kerogen inclusion with very low permeability. During exploitation, a boundary layer of flow forms in the kerogen, as shown by the textured brown strip, with fluid moving out of the inclusion, as indicated by the red arrows. The formation of the boundary layer can be analyzed in terms of the coordinate x that is normal to the interface between the matrix and the inclusions.
Fig. 2.
Fig. 2.
(Upper) Schematic of a nanoporous filter of width l in a fluid with pressure formula image in the region formula image and formula image in the region formula image. It is assumed that formula image, which causes fluid to flow in the negative direction, as shown by the blue arrows. Under the influence of a large pressure gradient, the structure of the filter is deformed and a boundary layer of finite width forms, as shown by the textured blue and gray region. (Lower) Corresponding pressure profile is shown by the solid purple line. The dashed purple lines show the pressure profile at later times as the boundary layer widens to stretch across the width of the filter until it reaches formula image. After this, the stabilization process begins, as shown by the dotted purple lines, and a constant pressure gradient across the filter is achieved eventually.
Fig. 3.
Fig. 3.
Plots of f (A) and formula image (B) for the nanoporous filtration example, for the case when formula image, for several different values of m. For the cases of formula image, the plots of f have finite support and monotonically decrease until reaching 0 at a finite value of ξ. (A, Inset) Zoomed-in region of one of the curves of f, which has a very small vertical range, demonstrating that the profiles of f are differentiable at the transition.
Fig. 4.
Fig. 4.
Profiles of f (A) and formula image (B) for the oil extraction problem, for the case of formula image, for several different values of m.
Fig. 5.
Fig. 5.
(A) Profiles of formula image for the gas extraction problem for the case of formula image for several different values of m. (B) Profiles of the rescaled permeability show a universality in behavior for different values of m.
Fig. 6.
Fig. 6.
Production data as a function of time for several oil and gas deposits in the Eagle Ford shale–Austin chalk system using data from Martin et al. (9) (A) and for several gas deposits in shales using data from Kulkarni (10) (B). Experimental data are shown using symbols, and for all cases, the data are well fit by a power law, with exponents in the range from −0.55 to −0.78, consistent with the model prediction.

References

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