1984
DOI: 10.1063/1.864544
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The effect of radius ratio on the stability of Couette flow and Taylor vortex flow

Abstract: Influence of a white noise at channel inlet on the parallel and wavy convective instabilities of Poiseuille-RayleighBénard flows Phys. Fluids 24, 084101 (2012) The role of boundaries in the magnetorotational instability Phys. Fluids 24, 074109 (2012) The onset of steady vortices in Taylor-Couette flow: The role of approximate symmetry Phys. Fluids 24, 064102 (2012) Transient growth in Rayleigh-Bénard-Poiseuille/Couette convection Phys. Fluids 24, 044103 (2012) Additional information on Phys. Fluids

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Cited by 57 publications
(43 citation statements)
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“…In figure 2 we show the Reynolds number at the instability onset as a function of k for different Ma; we define the critical Reynolds number, Re 1c , and corresponding wavenumber, k c , as the minimum of Re 1 at instability onset when optimised over k. In the incompressible limit, Ma ≈ 0, we obtain the well-known results of Rogers & Beard (1969) (see also DiPrima, Eagles & Ng 1984). By increasing gradually Ma from 0 to 5, we find that the effect of compressibility is to stabilise the system and increase the critical wavenumber k c slightly (see table 1 below); a similar behaviour for Re 1c and k c has also been observed when Ma > 5.…”
Section: Axisymmetric Instabilitiesmentioning
confidence: 55%
“…In figure 2 we show the Reynolds number at the instability onset as a function of k for different Ma; we define the critical Reynolds number, Re 1c , and corresponding wavenumber, k c , as the minimum of Re 1 at instability onset when optimised over k. In the incompressible limit, Ma ≈ 0, we obtain the well-known results of Rogers & Beard (1969) (see also DiPrima, Eagles & Ng 1984). By increasing gradually Ma from 0 to 5, we find that the effect of compressibility is to stabilise the system and increase the critical wavenumber k c slightly (see table 1 below); a similar behaviour for Re 1c and k c has also been observed when Ma > 5.…”
Section: Axisymmetric Instabilitiesmentioning
confidence: 55%
“…From DiPrima et al (1984), the corresponding critical Reynolds number and wavenumber are 317 and 0.46 respectively, in units of D and U C . These values are comparable to the square cavity flow data in table 1, highlighting once more the centrifugal character of the three-dimensional instabilities.…”
Section: Couette Flowsmentioning
confidence: 99%
“…The stability of such a flow has been widely studied and is often mentioned as a classical example of centrifugal instabilities. DiPrima, Eagles & Ng (1984) computed the critical values of the Reynolds number and corresponding axial wavenumber in Couette flow as a function of the radius ratio R 1 /R 2 for axisymmetric stationary modes. Note that their results were made dimensionless by scaling length with the gap width d = R 2 − R 1 and velocity with the inner cylinder velocity Ω 1 R 1 .…”
Section: Couette Flowsmentioning
confidence: 99%
“…The timescales for onset of such transient dynamic instabilities (<0.2 s) may be nearly instantaneous while investigating dynamic shear stress patterns within in vitro experiments. Highly complex flow behavior has been reported for annular Couette flows depending on radius and aspect (ratio of gap width to cylindrical height) ratios [37,38], Reynolds number and dynamics of rotation, such as transitions from circular Couette to Taylor Couette to wavy vortex to turbulent vortex flow [39]. Dynamics of such flow effects can be predicted numerically and explain the enhanced platelet activation in regions of complex flow with relatively smaller Reynolds numbers, but with presumably higher exposure times and collision frequencies.…”
Section: Taylor Number and Annular Flowmentioning
confidence: 97%
“…Such effects may therefore be substantially enhanced due to recirculation within Taylor vortices, where the duration of shear exposure and platelet-platelet collisions may be significantly increased relative to bulk flow. The shear stresses due to such flow effects can be effectively reproduced in Couette viscometers by appropriate choice of geometrical (e.g., radius ratio of the inner rotating and outer stationary cylinders, and aspect ratio, of the Couette viscometer) and experimental (e.g., rotational velocity and acceleration of the inner cylinder, viscosity of the fluid and overall shear stress) parameters [31,37]. Shear stress waveforms from numerical simulations may thus be reproduced in vitro with a dynamically controlled viscometer and thrombin generation from shear-stress activated platelets can be measured to determine thrombogenicity associated with PHV or recirculation devices.…”
Section: Plateletsmentioning
confidence: 99%