Challenge

Week 2 - Flow over a Cylinder.

introduction

In this, we will analyze flow over a cylinder for different Re for both steady and unsteady cases and find the Strouhal number which will show how Karman vortex street generated.

The Strouhal number is defined as St = fstD/U,

where fst is the vortex shedding frequency (or the Strouhal frequency) of a body at rest,

D is the diameter of the circular cylinder

U is the velocity of the ambient flow.

The Strouhal Number can be important when analyzing unsteady, oscillating flow problems. The Strouhal Number represents a measure of the ratio of the inertial forces due to the unsteadiness of the flow or local acceleration to the inertial forces due to changes in velocity from one point to another in the flow field.

Geometry

cylinder dia -2m

domain- 20x60m

Meshing

Nodes -31883

elements-6274

infliction layer-6

element size-0.2

solution setup

material - user-defined

density -1kg/m^3

dynamic viscosity -0.02 (to calculate for different Re )

type of solver is -pressure based laminar model

boundary condiction

initial velocity -1m/s

Results

Re 100

steady

residual plot

fat 270 iteration flow converged.

vortex shedding behind the cylinder.

coefficient of drag and lift plots

plot for vertex avrrage

it will show how vortex shedding behind the cylinder started, in this case at 150 iterations it started

unsteady case

residual plot

fat 40 iteration flow converged.

vortex shedding behind the cylinder.

coefficient of drag and lift plots

plot for vertex avrrage

it will show how vortex shedding behind the cylinder started

Plots of the coefficient of drag and lift for different Re

material - user-defined

density -1kg/m^3

dynamic viscosity -changes are made accordingly

type of solver is -pressure based laminar model

Re=10

lift plot

drag plot

Re=100

lift plot

drag plot

Re=1000

lift plot

drag plot

Re=10000

lift plot

drag plot

Re=100000

lift plot

drag plot

Expected results:-

1)in both cases flow converged, we have to look at the residuals plot to know the flow converges are not.

4) Mention the referred material is

material - user-defined

density -1kg/m^3

dynamic viscosity -0.02 (to calculate for different Re ) changes are made accordingly

*When Re is very low there no much change in Cl and Cd graph as the Re increases the Cl and Cd start fluctuating more as the number iteration increases, which indicates as very high velocity has high amount lift and drag.

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