Article contents
Numerical simulation of flow of a shear-thinning Carreau fluid over a transversely oscillating cylinder
Published online by Cambridge University Press: 01 July 2021
Abstract
Flow of a shear-thinning fluid over curved and moving geometries demands special attention owing to its industrial and biological relevance. The present study reports a numerical simulation of the motion of a Carreau fluid over a transversely oscillating cylinder for a range of oscillation amplitudes and frequencies at Reynolds number $Re = 100$, and compares the flow behaviour with that of a Newtonian fluid. The numerical solver uses the sharp-interface immersed boundary method to reconstruct the flow variables at the intercepted cells in the vicinity of the moving cylinder geometry. Synchronized vortex shedding is observed during the locked-in oscillation mode, whereas paired counter-rotating vortices are shed during the non-locked-in mode. The generation of vorticity and enstrophy variations in the Carreau and Newtonian fluids are compared. The vortex patterns in the Carreau fluid show a strong difference from those of the Newtonian fluid at higher amplitude of oscillation ($A^{*} = 1.2$). This difference in the flow structures is explained through the behaviour of the diffusion terms in the vorticity transport equation. Further, the effect of the Carreau fluid properties on the flow structures and vorticity dynamics are also discussed.
- Type
- JFM Papers
- Information
- Copyright
- © The Author(s), 2021. Published by Cambridge University Press
References
REFERENCES
Alam et al Supplementary Movie 1
The variations in viscosity during the cylinder oscillation cycles at A*=0.4, f*=0.6, Cu = 1.0 and n = 0.25.
Alam et al Supplementary Movie 2
The variations in viscosity during the cylinder oscillation cycles at A*=0.4, f*=1.0, Cu = 1.0 and n = 0.25.
Alam et al Supplementary Movie 3
The variations in viscosity during the cylinder oscillation cycles at A*=1.0, f*=1.0, Cu = 1.0 and n = 0.25.
Alam et al Supplementary Movie 4
The variations in viscosity during the cylinder oscillation cycles at A*=1.2, f*=1.0, Cu = 1.0 and n = 0.25.
Alam et al Supplementary Movie 5
The variations in viscosity during the cylinder oscillation cycles at A*=0.4, f*=1.0, Cu = 10.0 and n = 0.25.
Alam et al Supplementary Movie 6
The variations in vorticity during the cylinder oscillation cycles at A*=0.4, f*=0.6, Cu = 1.0 and n = 0.25.
Alam et al Supplementary Movie 7
The variations in vorticity during the cylinder oscillation cycles at A*=0.4, f*=1.0, Cu = 1.0 and n = 0.25.
Alam et al Supplementary Movie 8
The variations in vorticity during the cylinder oscillation cycles at A*=1.0, f*=1.0, Cu = 1.0 and n = 0.25.
- 21
- Cited by