Dissolution-driven convection in a heterogeneous porous medium

被引:14
|
作者
Salibindla, Ashwanth K. R. [1 ]
Subedi, Rabin [1 ]
Shen, Victor C. [1 ]
Masuk, Ashik U. M. [1 ]
Ni, Rui [1 ,2 ]
机构
[1] Penn State Univ, Dept Mech & Nucl Engn, University Pk, PA 16802 USA
[2] Johns Hopkins Univ, Dept Mech Engn, Baltimore, MD 21218 USA
关键词
Benard convection; convection; convection in porous media; RAYLEIGH-NUMBER CONVECTION; CARBON-DIOXIDE; ONSET; STORAGE; FLUID; STABILITY; DENSITIES; WATER; FLOW;
D O I
10.1017/jfm.2018.732
中图分类号
O3 [力学];
学科分类号
08 ; 0801 ;
摘要
Motivated by subsurface carbon sequestration, an experimental investigation of dissolution-driven Rayleigh-Darcy convection using two miscible fluids in a Hele-Shaw cell is conducted. A thin horizontal layer of circular impermeable discs is inserted to create an environment with heterogeneous and anisotropic permeability. The Sherwood number that measures the convective mass transfer rate between two fluids at the interface is linked to different parameters of the disc layer, including the disc size, spacing, layer permeability and its relative height with respect to the fluid interface. It is surprising that the convective mass transfer rate in our configuration is dominated by the disc spacing, but almost independent of either the disc size or the mean permeability of the layer. To explain this dependence, the convective mass transfer rate is decomposed into the number, velocity and density contrast of fingers travelling through the disc layer. Both the number and density contrast of fingers show dependences on the disc layer permeability, even though the product of them, the mass transfer rate, does not. In addition, the density contrast also shows a non-monotonic dependence on the disc spacing. The transition point is at a spacing that is close to the finger width. Based on this observation, a simple model based on mixing and scale competition is proposed, and it shows an excellent agreement with the experimental results.
引用
收藏
页码:61 / 79
页数:19
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