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Inertial flow transitions of a suspension in Taylor–Couette geometry
- Madhu V. Majji, Sanjoy Banerjee, Jeffrey F. Morris
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- Journal:
- Journal of Fluid Mechanics / Volume 835 / 25 January 2018
- Published online by Cambridge University Press:
- 28 November 2017, pp. 936-969
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- Article
- Export citation
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Experiments on the inertial flow transitions of a particle–fluid suspension in the concentric cylinder (Taylor–Couette) flow with rotating inner cylinder and stationary outer cylinder are reported. The radius ratio of the apparatus was
$\unicode[STIX]{x1D702}=d_{i}/d_{o}=0.877$ , where
$d_{i}$ and
$d_{o}$ are the diameters of inner and outer cylinders. The ratio of the axial length to the radial gap of the annulus
$\unicode[STIX]{x1D6E4}=L/\unicode[STIX]{x1D6FF}=20.5$ , where
$\unicode[STIX]{x1D6FF}=(d_{o}-d_{i})/2$ . The suspensions are formed of non-Brownian particles of equal density to the suspending fluid, of two sizes such that the ratio of annular gap to the mean particle diameter
$d_{p}$ was either
$\unicode[STIX]{x1D6FC}=\unicode[STIX]{x1D6FF}/d_{p}=30$ or
$100$ . For the experiments with
$\unicode[STIX]{x1D6FC}=100$ , the particle volume fraction was
$\unicode[STIX]{x1D719}=0.10$ and for the experiments with
$\unicode[STIX]{x1D6FC}=30$ ,
$\unicode[STIX]{x1D719}$ was varied over
$0\leqslant \unicode[STIX]{x1D719}\leqslant 0.30$ . The focus of the work is on determining the influence of particle loading and size on inertial flow transitions. The primary effects of the particles were a reduction of the maximum Reynolds number for the circular Couette flow (CCF) and several non-axisymmetric flow states not seen for a pure fluid with only inner cylinder rotation; here the Reynolds number is
$Re=\unicode[STIX]{x1D6FF}d_{i}\unicode[STIX]{x1D6FA}\unicode[STIX]{x1D70C}/2\unicode[STIX]{x1D707}_{s}$ , where
$\unicode[STIX]{x1D6FA}$ is the rotation rate of the inner cylinder and
$\unicode[STIX]{x1D70C}$ and
$\unicode[STIX]{x1D707}_{s}$ are the density and effective viscosity of the suspension. For purposes of maintaining uniform particle distribution, the rotation rate of the inner cylinder (or
$Re$ ) was decreased slowly from a state other than CCF to probe the transitions. When
$Re$ was decreased, pure fluid transitions from wavy Taylor vortex flow (WTV) to Taylor vortex flow (TVF) to CCF occurred. The suspension transitions differed. For
$\unicode[STIX]{x1D6FC}=30$ and
$0.05\leqslant \unicode[STIX]{x1D719}\leqslant 0.15$ , with reduction of
$Re$ , additional non-axisymmetric flow states, namely spiral vortex flow (SVF) and ribbons (RIB), were observed between TVF and CCF. At
$\unicode[STIX]{x1D719}=0.30$ , the flow transitions observed were only non-axisymmetric: from wavy spiral vortices (WSV) to SVF to CCF. The values of
$Re$ corresponding to each flow transition were observed to reduce with increase in particle loading for
$0\leqslant \unicode[STIX]{x1D719}\leqslant 0.30$ , with the initial transition away from CCF, for example, occurring at
$Re\approx 120$ for the pure fluid and
$Re\approx 75$ for the
$\unicode[STIX]{x1D719}=0.30$ suspension. When the particle size was reduced to yield
$\unicode[STIX]{x1D6FC}=100$ , at
$\unicode[STIX]{x1D719}=0.10$ , only the RIB (and no SVF) was observed between TVF and CCF.
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