Abstract

We perform a numerical and experimental study of immiscible two-phase flows within predominantly 2D transparent PDMS microfluidic domains with disordered pillar-like obstacles, that effectively serve as artificial porous structures. Using a high sensitivity pressure sensor at the flow inlet, we capture experimentally the pressure dynamics under fixed flow rate conditions as the fluid–fluid interface advances within the porous domain, while also monitoring the corresponding phase distribution patterns using optical microscopy. Our experimental study covers 4 orders of magnitude with respect to the injection flow rate and highlights the characteristics of immiscible displacement processes during the transition from the capillarity-controlled interface displacement regime at lower flow rates, where the pores are invaded sequentially in the form of Haines jumps, to the viscosity-dominated regime, where multiple pores are invaded simultaneously. In the capillary regime, we recover a clear correlation between the recorded inlet pressure and the pore-throat diameter invaded by the interface that follows the Young–Laplace equation, while during the transition to the viscous regime such a correlation is no longer evident due to multiple pore-throats being invaded simultaneously (but also due to significant viscous pressure drop along the inlet and outlet channels, that effectively mask capillary effects). The performed experimental study serves for the validation of a robust Level-Set model capable of explicitly tracking interfacial dynamics at sub-pore scale resolutions under identical flow conditions. The numerical model is validated against both well-established theoretical flow models, that account for the effects of viscous and capillary forces on interfacial dynamics, and the experimental results obtained using the developed microfluidic setup over a wide range of capillary numbers. Our results show that the proposed numerical model recovers very well the experimentally observed flow dynamics in terms of phase distribution patterns and inlet pressures, but also the effects of viscous flow on the apparent (i.e. dynamic) contact angles in the vicinity of the pore walls. For the first time in the literature, this work clearly shows that the proposed numerical approach has an undoubtable strong potential to simulate multiphase flow in porous domains over a wide range of Capillary numbers.

Highlights

  • IntroductionMultiphase flow in macroporous media (i.e. typical pore sizes greater than 50 nm) is a ubiquitous process of significant scientific and technological interest

  • Multiphase flow in macroporous media is a ubiquitous process of significant scientific and technological interest

  • We develop a microfluidic setup that allows for the simultaneous measurement of the inlet pressure during immiscible displacement within 2D PDMS porous-like domains at extremely high accuracy (i.e. ±20Pa which is sufficient for resolving both capillary and viscous pressure drop) and the corresponding phase distribution patterns using optical microscopy

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Summary

Introduction

Multiphase flow in macroporous media (i.e. typical pore sizes greater than 50 nm) is a ubiquitous process of significant scientific and technological interest. The developement of such micromodels followed relevant technological progress both in the fields of high-precision flow and pressure control allowing for the design of elaborate experimental study of immiscible flows in well-defined porous structures under a very wide range of flow conditions Experimental studies using such micromodels revealed the highly non-linear interaction between interfacial forces and the emergence of quite different flow regimes ranging from stable (piston-like) to fractal-like displacement patterns in the form of viscous and capillary ­fingers[19,28,29,30]. They were used to study flow regimes and their contribution to effective relative permeability curves in immiscible f­lows31–33,the effect of viscosity on sweeping ­efficiency[34], the correlation between capillary pressure and interfacial ­area[35], and more recently flows involving disconnected phases in the form of g­ anglia[27,36,37,38] that diverging significantly from the established Darcian flow description

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