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Reaction induced interfacial instability of miscible fluids in a channel

Published online by Cambridge University Press:  19 August 2021

Surya Narayan Maharana
Affiliation:
Department of Mathematics, Indian Institute of Technology Ropar, 140001 Rupnagar, India
Manoranjan Mishra*
Affiliation:
Department of Mathematics, Indian Institute of Technology Ropar, 140001 Rupnagar, India
*
Email address for correspondence: [email protected]

Abstract

When a less viscous miscible fluid displaces a more-viscous one under a pressure-driven channel flow, unstable Kelvin–Helmholtz (K–H)-type billows are formed at the miscible interface. In this paper, we investigate whether such instability can be induced by a simple ($\textbf {A}+ \textbf {B} \rightarrow \textbf {C}$)-type chemical reaction. Here a miscible solution of one reactant $\textbf {A}$ is displacing another isoviscous reactant $\textbf {B}$ and producing a more-viscous product $\textbf {C}$ at the reactive front. It is found that because of a local increase in viscosity gradient due to the formation of more-viscous product $\textbf {C}$, K–H-type billows are formed at the $\textbf {A}$$\textbf {C}$ interface. The changes in dynamical properties of such billows are examined by varying the governing parameters such as the mobility ratio $R_{c}$, Damköhler number $Da$, Péclet number $Pe$ and Reynolds number $Re$. Interestingly, we have found that even at high reaction rates (sufficiently large $Da$) for $R_{c}=1$, the interface remains stable and for larger values of $R_{c} (=3, 5)$ the K–H billows are observed. It is also noticed that a laminar horseshoe-type vortex develops near the wall at the channel inlet where the less-viscous reactant pushes the more-viscous product. We have computed numerically the onset time ($t_{on}$) of instability to understand the early-stage developments of the K–H billows. For different values of $Da$, we have shown the unstable and stable time zones in the ($t_{on}$$R_{c}$) space. The bipartite ($t_{on}$$R_{c}$) space also depicts the critical ($Da$-, $Pe$- and $Re$-dependent) $R_{c}$ value for which instability can be triggered in a finite desirable time. The delay in the onset of instability is observed with increasing $Pe$. Further it is shown that $t_{on}$ can be linearly scaled with $Pe$ to have a modified onset time ($t^{*}_{on}$), which establishes a proportionate dynamics with respect to $Pe$ in the early stages of the instability. Moreover, a reverse dependency of onset on lower $R_{c}$ values for higher Reynolds numbers is observed.

Type
JFM Papers
Copyright
© The Author(s), 2021. Published by Cambridge University Press

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References

REFERENCES

Balasubramaniam, R., Rashidnia, N., Maxworthy, T. & Kuang, J. 2005 Instability of miscible interfaces in a cylindrical tube. Phys. Fluids 17 (5), 052103.CrossRefGoogle Scholar
Brau, F. & De Wit, A. 2020 Influence of rectilinear vs radial advection on the yield of $A+B \rightarrow {C}$ reaction fronts: a comparison. J. Chem. Phys. 152 (5), 054716.CrossRefGoogle Scholar
Burghelea, T. & Frigaard, I. 2011 Unstable parallel flows triggered by a fast chemical reaction. J. Non-Newtonian Fluid Mech. 166 (9), 500514.CrossRefGoogle Scholar
Burghelea, T., Wielage-Burchard, K., Frigaard, I., Martinez, D.M. & Feng, J. 2007 A novel low inertia shear flow instability triggered by a chemical reaction. Phys. Fluids 19 (8), 083102.CrossRefGoogle Scholar
De Wit, A. 2020 Chemo-hydrodynamic patterns and instabilities. Annu. Rev. Fluid Mech. 52 (1), 531555.CrossRefGoogle Scholar
Ding, H., Spelt, P.D.M. & Shu, C. 2007 Diffuse interface model for incompressible two-phase flows with large density ratios. J. Comput. Phys. 226 (2), 20782095.CrossRefGoogle Scholar
Etrati, A. & Frigaard, I. 2018 Viscosity effects in density-stable miscible displacement flows: experiments and simulations. Phys. Fluids 30 (12), 123104.CrossRefGoogle Scholar
Gérard, T. & De Wit, A. 2009 Miscible viscous fingering induced by a simple $A+B \rightarrow C$ chemical reaction. Phys. Rev. E 79, 016308.CrossRefGoogle Scholar
Govindarajan, R. & Sahu, K.C. 2014 Instabilities in viscosity-stratified flow. Annu. Rev. Fluid Mech. 46 (1), 331353.CrossRefGoogle Scholar
Goyal, N. & Meiburg, E. 2006 Miscible displacements in Hele-Shaw cells: two-dimensional base states and their linear stability. J. Fluid Mech. 558, 329355.CrossRefGoogle Scholar
Jha, B., Cueto-Felgueroso, L. & Juanes, R. 2011 Fluid mixing from viscous fingering. Phys. Rev. Lett. 106, 194502.CrossRefGoogle ScholarPubMed
Lajeunesse, E., Martin, J., Rakotomalala, N., Salin, D. & Yortsos, Y.C. 1999 Miscible displacement in a Hele-Shaw cell at high rates. J. Fluid Mech. 398, 299319.CrossRefGoogle Scholar
Launay, G., Mignot, E., Riviere, N. & Perkins, R. 2017 An experimental investigation of the laminar horseshoe vortex around an emerging obstacle. J. Fluid Mech. 830, 257299.CrossRefGoogle Scholar
Leconte, M., Martin, J., Rakotomalala, N. & Salin, D. 2002 Pattern of reaction diffusion fronts in laminar flows. Phys. Rev. Lett. 90 (12), 128302.CrossRefGoogle Scholar
Matsumoto, Y. & Hoshino, M. 2004 Onset of turbulence induced by a Kelvin–Helmholtz vortex. Geophys. Res. Lett. 31 (2), L02807.CrossRefGoogle Scholar
Mishra, M., De Wit, A. & Sahu, K.C. 2012 Double diffusive effects on pressure-driven miscible displacement flows in a channel. J. Fluid Mech. 712, 579597.CrossRefGoogle Scholar
Miura, A. 1997 Compressible magnetohydrodynamic Kelvin–Helmholtz instability with vortex pairing in the two-dimensional transverse configuration. Phys. Plasmas 4 (8), 28712885.CrossRefGoogle Scholar
Nagatsu, Y., Hosokawa, Y., Kato, Y., Tada, Y. & Ueda, T. 2008 Miscible displacements with a chemical reaction in a capillary tube. AIChE J. 54 (3), 601613.CrossRefGoogle Scholar
Nagatsu, Y., Matsuda, K., Kato, Y. & Tada, Y. 2007 Experimental study on miscible viscous fingering involving viscosity changes induced by variations in chemical species concentrations due to chemical reactions. J. Fluid Mech. 571, 475493.CrossRefGoogle Scholar
Podgorski, T., Sostarecz, M.C., Zorman, S. & Belmonte, A. 2007 Fingering instabilities of a reactive micellar interface. Phys. Rev. E 76, 016202.CrossRefGoogle ScholarPubMed
Rashindia, N., Balasubramanium, R. & Schrder, R.T. 2004 The formation of spikes in the displacement of miscible fluids. Ann. N.Y. Acad. Sci. 1027 (1), 311316.Google Scholar
Reshadi, M. & Saidi, M.H. 2019 Tuning the dispersion of reactive solute by steady and oscillatory electroosmotic–Poiseuille flows in polyelectrolyte-grafted micro/nanotubes. J. Fluid Mech. 880, 73112.CrossRefGoogle Scholar
Riolfo, L.A., Nagatsu, Y., Iwata, S., Maes, R., Trevelyan, P.M.J. & De Wit, A. 2012 Experimental evidence of reaction-driven miscible viscous fingering. Phys. Rev. E 85, 015304.CrossRefGoogle ScholarPubMed
Sahu, K.C., Ding, H., Valluri, P. & Matar, O.K. 2009 a Linear stability analysis and numerical simulation of miscible two-layer channel flow. Phys. Fluids 21 (4), 042104.CrossRefGoogle Scholar
Sahu, K.C., Ding, H., Valluri, P. & Matar, O.K. 2009 b Pressure-driven miscible two-fluid channel flow with density gradients. Phys. Fluids 21 (4), 043603.CrossRefGoogle Scholar
Sharma, V., Pramanik, S., Chen, C.-Y. & Mishra, M. 2019 A numerical study on reaction-induced radial fingering instability. J. Fluid Mech. 862, 624638.CrossRefGoogle Scholar
Taghizadeh, E., Valdés-Parada, F.J. & Wood, B.D. 2020 Preasymptotic Taylor dispersion: evolution from the initial condition. J. Fluid Mech. 889, A5.CrossRefGoogle Scholar

Maharana and Mishra supplementary movie 1

Movie 1: With log mobility ratio R_c=0

Download Maharana and Mishra supplementary movie 1(Video)
Video 2.5 MB

Maharana and Mishra supplementary movie 2

Movie 2: With log mobility ratio R_C=1

Download Maharana and Mishra supplementary movie 2(Video)
Video 2.4 MB

Maharana and Mishra supplementary movie 3

Movie 3: With log mobility ratio R_c=5

Download Maharana and Mishra supplementary movie 3(Video)
Video 3.8 MB