The role of eddies inside pores in the transition from Darcy to Forchheimer flows

[1] We studied the role of intra-pore eddies, from viscous to inertial flows, in modifying continuum-scale flow inside pores. Flow regimes spanning Reynolds NumberRe∼ 0 to 1350 are divided into three zones – one zone follows Darcy flow, and the other two zones describe non-Darcy or Forchheimer flow. During viscous flows, i.e.,Re 1, and their growth leads to the deviation from Darcy's law and the emergence of Forchheimer flow manifested as a characteristic reduction in the apparent hydraulic conductivity Ka. The reduction in Ka is due to the narrowing of the flow channel which is a consequence of the growth in eddies. The two zones of Forchheimer flow correspond to the changes in rate of reduction in Ka, which in turn are due to the changes in eddy growth rate. Since the characteristics of Forchheimer flow are specific to pore geometry, our results partly explain why a variety of Forchheimer models are expected and needed for different porous media.

[1]  J. Auriault,et al.  High-Velocity Laminar and Turbulent Flow in Porous Media , 1999 .

[2]  Lynn F. Gladden,et al.  Local transitions in flow phenomena through packed beds identified by MRI , 2000 .

[3]  Adrian E. Scheidegger,et al.  The physics of flow through porous media , 1957 .

[4]  Ulrich Tallarek,et al.  Transition from creeping via viscous-inertial to turbulent flow in fixed beds. , 2006, Journal of chromatography. A.

[5]  M. Balhoff,et al.  A Predictive Pore-Scale Model for Non-Darcy Flow in Porous Media , 2009 .

[6]  G. Chauveteau,et al.  Régimes d'écoulement en milieu poreux et limite de la loi de Darcy , 1967 .

[7]  R. Lenormand,et al.  On the non-linear behavior of a laminar single-phase flow through two and three-dimensional porous media , 2004 .

[8]  M. Fourar,et al.  Physical splitting of nonlinear effects in high-velocity stable flow through porous media , 2006 .

[9]  Andro Mikelić,et al.  Polynomial Filtration Laws for Low Reynolds Number Flows Through Porous Media , 2010 .

[10]  Chiang C. Mei,et al.  The effect of weak inertia on flow through a porous medium , 1991, Journal of Fluid Mechanics.

[11]  S. Irmay On the theoretical derivation of Darcy and Forchheimer formulas , 1958 .

[12]  Richard A. Ketcham,et al.  Effects of inertia and directionality on flow and transport in a rough asymmetric fracture , 2009 .

[13]  Comparison of Quadratic and Power Law for Nonlinear Flow through Porous Media , 2008 .

[14]  J. Auriault,et al.  New insights on steady, non-linear flow in porous media , 1999 .

[15]  S. Whitaker The Forchheimer equation: A theoretical development , 1996 .

[16]  H. K. Moffatt Viscous and resistive eddies near a sharp corner , 1964, Journal of Fluid Mechanics.

[17]  William G. Gray,et al.  High velocity flow in porous media , 1987 .

[18]  Zhangxin Chen,et al.  Derivation of the Forchheimer Law via Homogenization , 2001 .

[19]  Beyond Anisotropy: Examining Non-Darcy Flow in Asymmetric Porous Media , 2010 .

[20]  Douglas Ruth,et al.  The microscopic analysis of high forchheimer number flow in porous media , 1993 .

[21]  M. Bayani Cardenas,et al.  Three‐dimensional vortices in single pores and their effects on transport , 2008 .

[22]  M. Panfilov,et al.  Singular nature of nonlinear macroscale effects in high-rate flow through porous media , 2003 .

[23]  J. Bear Dynamics of Fluids in Porous Media , 1975 .