Challenge

Rayleigh Taylor Instability simulation

AIM: To perform a Rayleigh Taylor instability simulation for two different mesh sizes.

THEORY:

Rayleigh Taylor Instability: It is an instability of an interface between two fluids of different densities which occurs when the lighter fluid pushes the heavier fluid.

Atwood Number: It is a dimensionless number in fluid dynamics used in the study of hydrodynamic instabilities.

`A=(ρ_1-ρ_2)/(ρ_1+ρ_2 )`

ρ1 = density of heavier fluid

ρ2 = density of lighter fluid

Some practical CFD models based on the mathematical analysis of Rayleigh Taylor waves:

  1. Plateau-Rayleigh Instability: This instability explains why and how a falling stream of fluid breaks up into smaller packets with the same volume but less surface area. It is related to the Rayleigh Taylor instability.
  2. Richtmyer–Meshkov Instability: The Richtmyer–Meshkov instability (RMI) occurs when two fluids of different density are impulsively accelerated. Normally this is by the passage of a shock wave.

PROCEDURE:

Geometry: The geometry was constructed in SpaceClaim for both the top and bottom fluid surfaces having dimensions 20mm*20mm. Using the pull tool, the geometry was converted to a 2-D surface. And in order to have a conformal mesh, share topology was enabled.

Mesh: Mesh sizes were taken as 0.5 mm and 0.2 mm.

Mesh size = 0.5 mm

Mesh size = 0.2 mm

Setup and Solution:

Results:

Case 1:

Mesh size = 0.5 mm

Primary phase – Air

Secondary phase – Water

Time step size = 0.005 s

No of time steps = 1000

Link for animation file: https://drive.google.com/file/d/1k0WR-LJzOs-BqFUAK2g8MpbPK0ZNL_9L/view?usp=sharing

Atwood number calculation:

ρ1 = 998.2 kg/m3

ρ2 = 1.225 kg/m3

`A=(998.2-1.225)/(998.2+1.225)`

`A=0.997`

Case 2:

Mesh size = 0.2 mm

Primary phase – Air

Secondary phase – Water

Time step size = 0.005 s

No of time steps = 1000

Link for animation file: https://drive.google.com/file/d/1k8d5p3kF9WREHiBN9aU_kno2Xx2rofIB/view?usp=sharing

Atwood number calculation:

ρ1 = 998.2 kg/m3

ρ2 = 1.225 kg/m3

`A=(998.2-1.225)/(998.2+1.225)`

`A=0.997`

Case 3:

Mesh size = 0.2 mm

Primary phase – User-defined fluid

Secondary phase – Water

Time step size = 0.005 s

No of time steps = 1000

Link for animation file: https://drive.google.com/file/d/1kAbkVyIu00B25uopUbKKRoa6b40bLRig/view?usp=sharing

Atwood number calculation:

ρ1 = 998.2 kg/m3

ρ2 = 400 kg/m3

`A=(998.2-400)/(998.2+400)`

`A=0.427`

Conclusion:

  • A finer mesh captures the instabilities more properly than a coarse mesh.
  • A transient approach is preferred since the instability simulation occurs in an unpredictable manner and changes as a function of time.
  • Higher Atwood number refers to a higher rate of mixing, and the instability begins with a bubble-like formation.
  • Lower Atwood number refers to a lower rate of mixing, and the instability begins with finger-like formations.
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