Week 2 - Flow over a Cylinder.

Aim:

To Simulate the flow over a cylinder and explain the phenomenon of Karman vortex street.  

Objective:

1.To Calculate the coefficient of drag and lift over a cylinder by setting the Reynolds number to 10,100,1000,10000 & 100000. (Run with steady solver)

2.Simulate the flow with the steady and unsteady case and calculate the Strouhal Number for Re= 100. 

 

Introduction:

Vortex shadding:

vortex shedding is an oscillating flow that takes place when a fluid such as air or water flows past a bluff (as opposed to streamlined) body at certain velocities, depending on the size and shape of the body. In this flow, vortices are created at the back of the body and detach periodically from either side of the body forming a Von Karman vortex street. The fluid flow past the object creates alternating low-pressure vortices on the downstream side of the object. The object will tend to move toward the low-pressure zone.

If the bluff structure is not mounted rigidly and the frequency of vortex shedding matches the resonance frequency of the structure, then the structure can begin to resonate, vibrating with harmonic oscillations driven by the energy of the flow. This vibration is the cause for overhead power line wires humming in the wind, and for the fluttering of automobile whip radio antennas  at some speeds. Tall chimneys constructed of thin-walled steel tubes can be sufficiently flexible that, in air flow with a speed in the critical range, vortex shedding can drive the chimney into violent oscillations that can damage or destroy the chimney.

Procedure:

Geometry:

A plate with the dimension of 20*60m is created using spaceclaim.

Now,we want to simulate effect of fluid flow over cylinder, select the circle and delete it.

Meshing:

1.select the edges of geometry and named them as inlet,outlet ,wall and symmetry.

2.Now select the body and go to mesh and click on generate mesh with mesh size 0.25 m.To ensure triangular mesh, go to mesh > insert > select triangular mesh type.

         

3.After generating mesh,it is seen that size of cirle looks distoreted.

go to mesh > sizing > select circular edge > deffinition >type > no,of divisions >36.

4.To capture better results near cylinder wall, go to mesh > inflation > select the body and edge > inflation option : 1st layer thickness >1 st layer height :5e-3 m >maximum layer :6

1. select laminar flow inside the viscous model.

2.As we wanted to customimize material property for simulation, go to materials > fluent database > select the material (air) > copy it> rename the name of material.

 

Boundary Condition:

Outlet : gauge pressure = 0 Pa.

wall : no slip condition.

 

Refference values:

Steady state simulation:

1.Reynolds number = 10.

velocity = 1 m/s.

density = 1 kg/m3.

viscosity = 0.02 Pa-s.

 

Residual plot:

Monitor point velocity:

monitor point: A point is created at 8 m in x direction from the axis of cylinder to check velocity.

Coefficient of drag:

Lift Coefficient:

      

Velocity contour:

       

Pressure contour:

      

2.Reynolds number = 100.

velocity = 10 m/s.

density = 1 kg/m3.

viscosity = 0.02 Pa-s.

 

Residual plot:

 

Monitor point velocity:

monitor point: A point is created at 8 m in x direction from the axis of cylinder to check velocity.

Coefficient of drag:

      

 

Lift Coefficient:

      

Velocity contour:

       

pressure contour:

       

3.Reynolds number = 1000.

velocity = 100 m/s.

density = 1 kg/m3.

viscosity = 0.02 Pa-s.

 

Residual plot:

Monitor point velocity:

      

 

Coefficient of drag:

Lift Coefficient:

Velocity contour:

       

pressure conture ;

4.Reynolds number = 10000.

velocity = 1000 m/s.

density = 1 kg/m3.

viscosity = 0.02 Pa-s.

 Residual plot:

Monitor point velocity:

      

Coefficient of drag:

 

Lift Coefficient:

Velocity contour:

pressure contour ;

5.Reynolds number = 100000.

velocity = 10000 m/s.

density = 1 kg/m3.

viscosity = 0.02 Pa-s.

 

Residual plot:

Monitor point velocity ;

Coefficient of drag:

      

Lift Coefficient:

 

Velocity contour:

Pressure contour:

 

Unstaedy state solver:

Reynolds number = 100.

velocity = 10 m/s.

density = 1 kg/m3.

viscosity = 0.02 Pa-s.

 

Residual plot:

Monitor point velocity:

      

Coefficient of drag:

Lift Coefficient:

Velocity contour:

Pressure contour:

 

 Result:

    Values of coefficient of drag and lift coefficient for respective reynolds number is tabulated as follows:

Conclusion:

1.When fluid flows over cylinder, wake region is formed next to cylinder due to decrease in pressure and recirculation of flow occures and hence flow separation occures.

2.As flow over cylinder is being transient meaning time dependent phenomenon, we are unable to observe flow separation at low reynolds no.(say 50).

3.In this assignment we have kept all parameters constant and have only varried velocity to change reynolds number. So as the reynolds no. increases coefficient of drag decreases.however after reynolds no. = 4000, flow is turbulent and hence coefficient of drag is lower.

4.Strauhal no. calculated for unsteady state with reynolds no.= 100 is 0.112.

FLOW OVER A CYLINDER ;

https://drive.google.com/file/d/1R-W-4W_vN5XbUT7pIDHOTL4Em0g8Gup6/view?usp=sharing

FLOW OVER A CYINDER ANIMATION

https://youtu.be/udD_0TrzH58