The centre-mode instability of viscoelastic plane Poiseuille flow
A modal stability analysis shows that plane Poiseuille flow of an Oldroyd-B fluid becomes unstable to a ‘centre mode’ with phase speed close to the maximum base-flow velocity, $U_{max}$. The governing dimensionless groups are the Reynolds number $Re = \rho U_{max} H/\eta$, the elasticity number $E =...
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description | A modal stability analysis shows that plane Poiseuille flow of an Oldroyd-B fluid becomes unstable to a ‘centre mode’ with phase speed close to the maximum base-flow velocity, $U_{max}$. The governing dimensionless groups are the Reynolds number $Re = \rho U_{max} H/\eta$, the elasticity number $E = \lambda \eta /(H^2 \rho )$ and the ratio of solvent to solution viscosity $\beta = \eta _s/\eta$; here, $\lambda$ is the polymer relaxation time, $H$ is the channel half-width and $\rho$ is the fluid density. For experimentally relevant values (e.g. $E \sim 0.1$ and $\beta \sim 0.9$), the critical Reynolds number, $Re_c$, is around $200$, with the associated eigenmodes being spread out across the channel. For $E(1-\beta ) \ll 1$, with $E$ fixed, corresponding to strongly elastic dilute polymer solutions, $Re_c \propto (E(1-\beta ))^{-3/2}$ and the critical wavenumber $k_c \propto (E(1-\beta ))^{-1/2}$. The unstable eigenmode in this limit is confined in a thin layer near the channel centreline. These features are largely analogous to the centre-mode instability in viscoelastic pipe flow (Garg et al., Phys. Rev. Lett., vol. 121, 2018, 024502), and suggest a universal linear mechanism underlying the onset of turbulence in both channel and pipe flows of sufficiently elastic dilute polymer solutions. Although the centre-mode instability continues down to $\beta \sim 10^{-2}$ for pipe flow, it ceases to exist for $\beta < 0.5$ in channels. Whereas inertia, elasticity and solvent viscous effects are simultaneously required for this instability, a higher viscous threshold is required for channel flow. Further, in the opposite limit of $\beta \rightarrow 1$, the centre-mode instability in channel flow continues to exist at $Re \approx 5$, again in contrast to pipe flow where the instability ceases to exist below $Re \approx 63$, regardless of $E$ or $\beta$. Our predictions are in reasonable agreement with experimental observations for the onset of turbulence in the flow of polymer solutions through microchannels. |
doi_str_mv | 10.1017/jfm.2021.60 |
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The governing dimensionless groups are the Reynolds number $Re = \rho U_{max} H/\eta$, the elasticity number $E = \lambda \eta /(H^2 \rho )$ and the ratio of solvent to solution viscosity $\beta = \eta _s/\eta$; here, $\lambda$ is the polymer relaxation time, $H$ is the channel half-width and $\rho$ is the fluid density. For experimentally relevant values (e.g. $E \sim 0.1$ and $\beta \sim 0.9$), the critical Reynolds number, $Re_c$, is around $200$, with the associated eigenmodes being spread out across the channel. For $E(1-\beta ) \ll 1$, with $E$ fixed, corresponding to strongly elastic dilute polymer solutions, $Re_c \propto (E(1-\beta ))^{-3/2}$ and the critical wavenumber $k_c \propto (E(1-\beta ))^{-1/2}$. The unstable eigenmode in this limit is confined in a thin layer near the channel centreline. These features are largely analogous to the centre-mode instability in viscoelastic pipe flow (Garg et al., Phys. Rev. Lett., vol. 121, 2018, 024502), and suggest a universal linear mechanism underlying the onset of turbulence in both channel and pipe flows of sufficiently elastic dilute polymer solutions. Although the centre-mode instability continues down to $\beta \sim 10^{-2}$ for pipe flow, it ceases to exist for $\beta < 0.5$ in channels. Whereas inertia, elasticity and solvent viscous effects are simultaneously required for this instability, a higher viscous threshold is required for channel flow. Further, in the opposite limit of $\beta \rightarrow 1$, the centre-mode instability in channel flow continues to exist at $Re \approx 5$, again in contrast to pipe flow where the instability ceases to exist below $Re \approx 63$, regardless of $E$ or $\beta$. Our predictions are in reasonable agreement with experimental observations for the onset of turbulence in the flow of polymer solutions through microchannels.</description><identifier>ISSN: 0022-1120</identifier><identifier>EISSN: 1469-7645</identifier><identifier>DOI: 10.1017/jfm.2021.60</identifier><language>eng</language><publisher>Cambridge, UK: Cambridge University Press</publisher><subject>Base flow ; Channel flow ; Dilution ; Elasticity ; Experiments ; Flow stability ; Flow velocity ; Fluid dynamics ; Fluid flow ; Inertia ; Instability ; JFM Papers ; Laminar flow ; Microchannels ; Phase velocity ; Pipe flow ; Polymers ; Relaxation time ; Reynolds number ; Solvents ; Stability analysis ; Turbulence ; Turbulent flow ; Viscoelasticity ; Viscosity ; Wavelengths</subject><ispartof>Journal of fluid mechanics, 2021-03, Vol.915, Article A43</ispartof><rights>The Author(s), 2021. Published by Cambridge University Press</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c299t-fcefa957ff71092ece54ff8ab7db639ae5d02e32141663948a2cb33489fd81143</citedby><cites>FETCH-LOGICAL-c299t-fcefa957ff71092ece54ff8ab7db639ae5d02e32141663948a2cb33489fd81143</cites><orcidid>0000-0003-0233-7494 ; 0000-0001-7935-5805 ; 0000-0001-8215-5695 ; 0000-0003-4314-3602</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.cambridge.org/core/product/identifier/S0022112021000604/type/journal_article$$EHTML$$P50$$Gcambridge$$H</linktohtml><link.rule.ids>164,314,780,784,27924,27925,55628</link.rule.ids></links><search><creatorcontrib>Khalid, Mohammad</creatorcontrib><creatorcontrib>Chaudhary, Indresh</creatorcontrib><creatorcontrib>Garg, Piyush</creatorcontrib><creatorcontrib>Shankar, V.</creatorcontrib><creatorcontrib>Subramanian, Ganesh</creatorcontrib><title>The centre-mode instability of viscoelastic plane Poiseuille flow</title><title>Journal of fluid mechanics</title><addtitle>J. Fluid Mech</addtitle><description>A modal stability analysis shows that plane Poiseuille flow of an Oldroyd-B fluid becomes unstable to a ‘centre mode’ with phase speed close to the maximum base-flow velocity, $U_{max}$. The governing dimensionless groups are the Reynolds number $Re = \rho U_{max} H/\eta$, the elasticity number $E = \lambda \eta /(H^2 \rho )$ and the ratio of solvent to solution viscosity $\beta = \eta _s/\eta$; here, $\lambda$ is the polymer relaxation time, $H$ is the channel half-width and $\rho$ is the fluid density. For experimentally relevant values (e.g. $E \sim 0.1$ and $\beta \sim 0.9$), the critical Reynolds number, $Re_c$, is around $200$, with the associated eigenmodes being spread out across the channel. For $E(1-\beta ) \ll 1$, with $E$ fixed, corresponding to strongly elastic dilute polymer solutions, $Re_c \propto (E(1-\beta ))^{-3/2}$ and the critical wavenumber $k_c \propto (E(1-\beta ))^{-1/2}$. The unstable eigenmode in this limit is confined in a thin layer near the channel centreline. These features are largely analogous to the centre-mode instability in viscoelastic pipe flow (Garg et al., Phys. Rev. Lett., vol. 121, 2018, 024502), and suggest a universal linear mechanism underlying the onset of turbulence in both channel and pipe flows of sufficiently elastic dilute polymer solutions. Although the centre-mode instability continues down to $\beta \sim 10^{-2}$ for pipe flow, it ceases to exist for $\beta < 0.5$ in channels. Whereas inertia, elasticity and solvent viscous effects are simultaneously required for this instability, a higher viscous threshold is required for channel flow. Further, in the opposite limit of $\beta \rightarrow 1$, the centre-mode instability in channel flow continues to exist at $Re \approx 5$, again in contrast to pipe flow where the instability ceases to exist below $Re \approx 63$, regardless of $E$ or $\beta$. Our predictions are in reasonable agreement with experimental observations for the onset of turbulence in the flow of polymer solutions through microchannels.</description><subject>Base flow</subject><subject>Channel flow</subject><subject>Dilution</subject><subject>Elasticity</subject><subject>Experiments</subject><subject>Flow stability</subject><subject>Flow velocity</subject><subject>Fluid dynamics</subject><subject>Fluid flow</subject><subject>Inertia</subject><subject>Instability</subject><subject>JFM Papers</subject><subject>Laminar flow</subject><subject>Microchannels</subject><subject>Phase velocity</subject><subject>Pipe flow</subject><subject>Polymers</subject><subject>Relaxation time</subject><subject>Reynolds number</subject><subject>Solvents</subject><subject>Stability analysis</subject><subject>Turbulence</subject><subject>Turbulent flow</subject><subject>Viscoelasticity</subject><subject>Viscosity</subject><subject>Wavelengths</subject><issn>0022-1120</issn><issn>1469-7645</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2021</creationdate><recordtype>article</recordtype><sourceid>8G5</sourceid><sourceid>ABUWG</sourceid><sourceid>AFKRA</sourceid><sourceid>AZQEC</sourceid><sourceid>BENPR</sourceid><sourceid>CCPQU</sourceid><sourceid>DWQXO</sourceid><sourceid>GNUQQ</sourceid><sourceid>GUQSH</sourceid><sourceid>M2O</sourceid><recordid>eNptkF1LwzAYhYMoOKdX_oGCl9L55qNNczmGTmGgF_M6pOkbzWibmXTK_r0dG3jj1eHAwznwEHJLYUaByoeN62YMGJ2VcEYmVJQql6UozskEgLGcUgaX5CqlDQDloOSEzNefmFnsh4h5FxrMfJ8GU_vWD_ssuOzbJxuwNWnwNtu2psfsLfiEO9-2mLk2_FyTC2fahDennJL3p8f14jlfvS5fFvNVbplSQ-4sOqMK6ZykoBhaLIRzlallU5dcGSwaYMgZFbQcu6gMszXnolKuqSgVfErujrvbGL52mAa9CbvYj5eaFQCcg1RqpO6PlI0hpYhOb6PvTNxrCvrgSI-O9MGRLmGk8xNtujr65gP_Rv_jfwEiWWiK</recordid><startdate>20210312</startdate><enddate>20210312</enddate><creator>Khalid, Mohammad</creator><creator>Chaudhary, Indresh</creator><creator>Garg, Piyush</creator><creator>Shankar, V.</creator><creator>Subramanian, Ganesh</creator><general>Cambridge University Press</general><scope>AAYXX</scope><scope>CITATION</scope><scope>3V.</scope><scope>7TB</scope><scope>7U5</scope><scope>7UA</scope><scope>7XB</scope><scope>88I</scope><scope>8FD</scope><scope>8FE</scope><scope>8FG</scope><scope>8FK</scope><scope>8G5</scope><scope>ABJCF</scope><scope>ABUWG</scope><scope>AFKRA</scope><scope>ARAPS</scope><scope>AZQEC</scope><scope>BENPR</scope><scope>BGLVJ</scope><scope>BHPHI</scope><scope>BKSAR</scope><scope>C1K</scope><scope>CCPQU</scope><scope>DWQXO</scope><scope>F1W</scope><scope>FR3</scope><scope>GNUQQ</scope><scope>GUQSH</scope><scope>H8D</scope><scope>H96</scope><scope>HCIFZ</scope><scope>KR7</scope><scope>L.G</scope><scope>L6V</scope><scope>L7M</scope><scope>M2O</scope><scope>M2P</scope><scope>M7S</scope><scope>MBDVC</scope><scope>P5Z</scope><scope>P62</scope><scope>PCBAR</scope><scope>PQEST</scope><scope>PQQKQ</scope><scope>PQUKI</scope><scope>PTHSS</scope><scope>Q9U</scope><scope>S0W</scope><orcidid>https://orcid.org/0000-0003-0233-7494</orcidid><orcidid>https://orcid.org/0000-0001-7935-5805</orcidid><orcidid>https://orcid.org/0000-0001-8215-5695</orcidid><orcidid>https://orcid.org/0000-0003-4314-3602</orcidid></search><sort><creationdate>20210312</creationdate><title>The centre-mode instability of viscoelastic plane Poiseuille flow</title><author>Khalid, Mohammad ; 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Fluid Mech</addtitle><date>2021-03-12</date><risdate>2021</risdate><volume>915</volume><artnum>A43</artnum><issn>0022-1120</issn><eissn>1469-7645</eissn><abstract>A modal stability analysis shows that plane Poiseuille flow of an Oldroyd-B fluid becomes unstable to a ‘centre mode’ with phase speed close to the maximum base-flow velocity, $U_{max}$. The governing dimensionless groups are the Reynolds number $Re = \rho U_{max} H/\eta$, the elasticity number $E = \lambda \eta /(H^2 \rho )$ and the ratio of solvent to solution viscosity $\beta = \eta _s/\eta$; here, $\lambda$ is the polymer relaxation time, $H$ is the channel half-width and $\rho$ is the fluid density. For experimentally relevant values (e.g. $E \sim 0.1$ and $\beta \sim 0.9$), the critical Reynolds number, $Re_c$, is around $200$, with the associated eigenmodes being spread out across the channel. For $E(1-\beta ) \ll 1$, with $E$ fixed, corresponding to strongly elastic dilute polymer solutions, $Re_c \propto (E(1-\beta ))^{-3/2}$ and the critical wavenumber $k_c \propto (E(1-\beta ))^{-1/2}$. The unstable eigenmode in this limit is confined in a thin layer near the channel centreline. These features are largely analogous to the centre-mode instability in viscoelastic pipe flow (Garg et al., Phys. Rev. Lett., vol. 121, 2018, 024502), and suggest a universal linear mechanism underlying the onset of turbulence in both channel and pipe flows of sufficiently elastic dilute polymer solutions. Although the centre-mode instability continues down to $\beta \sim 10^{-2}$ for pipe flow, it ceases to exist for $\beta < 0.5$ in channels. Whereas inertia, elasticity and solvent viscous effects are simultaneously required for this instability, a higher viscous threshold is required for channel flow. Further, in the opposite limit of $\beta \rightarrow 1$, the centre-mode instability in channel flow continues to exist at $Re \approx 5$, again in contrast to pipe flow where the instability ceases to exist below $Re \approx 63$, regardless of $E$ or $\beta$. Our predictions are in reasonable agreement with experimental observations for the onset of turbulence in the flow of polymer solutions through microchannels.</abstract><cop>Cambridge, UK</cop><pub>Cambridge University Press</pub><doi>10.1017/jfm.2021.60</doi><tpages>40</tpages><orcidid>https://orcid.org/0000-0003-0233-7494</orcidid><orcidid>https://orcid.org/0000-0001-7935-5805</orcidid><orcidid>https://orcid.org/0000-0001-8215-5695</orcidid><orcidid>https://orcid.org/0000-0003-4314-3602</orcidid></addata></record> |
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subjects | Base flow Channel flow Dilution Elasticity Experiments Flow stability Flow velocity Fluid dynamics Fluid flow Inertia Instability JFM Papers Laminar flow Microchannels Phase velocity Pipe flow Polymers Relaxation time Reynolds number Solvents Stability analysis Turbulence Turbulent flow Viscoelasticity Viscosity Wavelengths |
title | The centre-mode instability of viscoelastic plane Poiseuille flow |
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