2009
DOI: 10.1063/1.3116285
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Linear stability analysis and numerical simulation of miscible two-layer channel flow

Abstract: The stability of miscible two-fluid flow in a horizontal channel is examined. The flow dynamics are governed by the continuity and Navier-Stokes equations coupled to a convective-diffusion equation for the concentration of the more viscous fluid through a concentration-dependent viscosity.Our analysis of the flow in the linear regime delineates the presence of convective and absolute instabilities and identifies the vertical gradients of viscosity perturbations as the main destabilizing influence in agreement … Show more

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Cited by 91 publications
(85 citation statements)
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“…The numerical procedure and boundary conditions used to solve equations (2.7)-(2.10) are described in § 3. Note that, for the boundary conditions used here, when one of the log mobility ratios (either R f or R s ) is set to zero or δ = 1, the above equations (2.7)-(2.11) reduce to a single solute model, the flow dynamics of which has been discussed using a Navier-Stokes solver by Sahu et al (2009a). To have an idea of the order of magnitude of the log mobility ratios for real systems, we note that, if, for instance, the invading fluid is methanol (kinematic viscosity ν = 0.6704 cSt) and the displaced fluid is a mixture of ethylene glycol, acetone and methanol (ν = 0.5472 cSt) (Kalidas & Laddha 1964), we get R s = 3 and R f = −3.24.…”
Section: Mathematical Formulationmentioning
confidence: 99%
See 1 more Smart Citation
“…The numerical procedure and boundary conditions used to solve equations (2.7)-(2.10) are described in § 3. Note that, for the boundary conditions used here, when one of the log mobility ratios (either R f or R s ) is set to zero or δ = 1, the above equations (2.7)-(2.11) reduce to a single solute model, the flow dynamics of which has been discussed using a Navier-Stokes solver by Sahu et al (2009a). To have an idea of the order of magnitude of the log mobility ratios for real systems, we note that, if, for instance, the invading fluid is methanol (kinematic viscosity ν = 0.6704 cSt) and the displaced fluid is a mixture of ethylene glycol, acetone and methanol (ν = 0.5472 cSt) (Kalidas & Laddha 1964), we get R s = 3 and R f = −3.24.…”
Section: Mathematical Formulationmentioning
confidence: 99%
“…In the food processing industries cleaning involves the removal of a highly viscous fluid by water. The stability of this type of two-phase flow in a channel or pipe has been widely investigated both theoretically (Ranganathan & Govindarajan 2001;Selvam et al 2007;Sahu et al 2009a; and experimentally (Hickox 1971;Hu & Joseph 1989;Joseph & Renardy 1992;Joseph et al 1997). Linear stability analyses of displacement flows in porous media (Saffman & Taylor 1958;Chouke, Van Meurs & Van Der Pol 1959;Tan & Homsy 1986) explain that, if the displacing fluid is less viscous than the displaced one, the interface separating them becomes unstable and a fingering pattern develops at the interface.…”
Section: Introductionmentioning
confidence: 99%
“…In pressure-driven two-layer/core-annular flows, several authors have conducted linear stability analyses by considering the fluids to be immiscible 4,[6][7][8] and miscible. 3,[9][10][11][12] This problem was also studied by many researchers experimentally 13,14 and numerically. [15][16][17][18] In miscible core-annular flows, the thickness of the more viscous fluid layer left on the pipe walls and the speed of the propagating "finger" were experimentally investigated by many authors [19][20][21][22][23] and the axisymmetric and "corkscrew" patterns were found.…”
Section: Introductionmentioning
confidence: 99%
“…3 The interface between the two fluids becomes unstable forming Yihtype instability for immiscible 4 and Kelvin-Helmholtz (KH) type instabilities and "roll-up" structures for miscible flows. A review of the phenomenon occurring in porous media (commonly known as viscous fingering) can be found in Ref.…”
Section: Introductionmentioning
confidence: 99%
“…Sahu et al 37 showed that the above system becomes absolutely unstable for a certain range of parameters and have indicated the region of absolute and convective instabilities in the Reynolds number and viscosity ratio space. There are also several investigations 29,30,[38][39][40][41][42][43][44][45][46][47][48] not relevant to the present study (but worth mentioning in the present context) that deals with stability characteristics of viscosity stratified flows in rigid channels/pipes, involving the displacement of one fluid by another. The interesting features and the type of instabilities displayed by these flow systems with boundaries as either rigid walls or rigid circular pipes suggest that it is worth analyzing the analogous flow systems in configurations with velocity slip at the boundaries.…”
Section: Introductionmentioning
confidence: 99%