Project

Pipe flow Simulation with line probes in SolidWorks

Aim: To do the simulation of pipe flow using line probes in SolidWorks Flow Simulation

Objective:

  • Run a pipe flow simulation with an inlet Reynolds number of 100,1000 and 10000.
  • For each of these cases do the following:
  1. Place line probes at 95%, 90% and 85% of the pipe length.
  2. Compare the normalized velocity profile at each of these locations.
  3. Normalize the velocity profile by the inlet velocity.

Introduction:

Laminar flow:

  • Laminar flow occurs when the fluid flows in infinitesimal parallel layers with no disruption between them.
  • In Laminar flows, fluid layers slide in parallel with no eddies, swirls or currents normal to the flow itself.

Fig. Laminar flow in closed pipe

Turbulent flow:

  • In fluid dynamics, a turbulent means irregular flows in which eddies, swirls, and other flow instabilities occur.
  • Turbulence is commonly observed in everyday phenomena such as fast flowing rivers, smoke from chimney, etc.

Fig. Turbulent flow in closed pipe

Reynold’s number:

  • The Reynold’s number (Re) is a dimensionless number expressing the ratio between inertial force and viscous force.
  • The Reynold’s number is a mathematically defined as:

  • At low values of Re, the flow is Laminar. But when Re exceeds a certain threshold, semi-developed turbulence occurs in the flow, this regime is referred to as Transition regime and occurs for a certain range of the Reynold’s number.
  • Finally, over a certain value of Re, the flow becomes fully

Viscosity:

  • The resistance of a fluid to flow when subjected to a force is called Viscosity.

Dynamic Viscosity

  • The unit of measurement of Dynamic Viscosity is Pa s or N s/m2
  • Dynamic Viscosity is also known as Absolute viscosity.

Kinematic Viscosity

  • The unit of measurement of Kinematic Viscosity is m2/s
  • Kinematic Viscosity is also known as Diffusivity of Momentum.

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Specification of problem:

Diameter of pipe = 0.04m

Thickness of pipe = 0.001m

At 25° C

µ = 0.00089 Pa s or 0.00089 N s/m2

= 1000 kg/m3

Length of pipe L = 1m

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Calculations:

For Reynold’s number Re =100

Therefore,

V = 0.00223 m/s ------------------------------(CASE 1)

Similarly, for Re = 1000

V = 0.0223 m/s------------------------------- (CASE 2)

And for, Re = 10000

V = 0.223 m/s--------------------------------- (CASE 3)

Reynold’s number (Re)

Flow velocity V (m/s)

100

0.00223

1000

0.0223

10000

0.223

Procedure for Simulation for all the 3 cases:

  • Modelling of pipe in SolidWorks

  • Place the line probes at 85%, 90% and 95% of the pipe length by using the sketch command.
  • Go to the Flow Simulation from SolidWorks Add-ins

  • Create a new project in Flow Simulation

  • Create the lids at the end faces of the pipe for watertight enclosed volume which is mandatory for CFD analysis.

  • Now form general settings set the analysis type as shown in the following figure:

  • In this project we will consider water as fluid for all the 3 cases and the flow characteristic be Laminar and Turbulent.

  • Wall Condition is set as below:

  • Initial condition parameters are set as below:

  • Set boundary conditions at inlet, outlet and inner wall of the pipe.
  • Insert XY plots for all the 3 cases
  • Insert Cut plots for all the 3 cases

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Case No: 1 (Re= 100)

For inlet boundary condition:

Inlet velocity = 0.0023 m/s

For outlet boundary condition:

Static pressure= 101325 Pa

Temperature = 293.2 K

Third Boundary condition:

Real wall

Results for Case No : 1 (Re = 100)

Cut plot for 85% pipe length

Cut plot for 90% of pipe length Cut plot at 95% of pipe length

Velocity plots for Case : 1

Fig. Shows the Velocity plot for Case:1 Re=100, v = 0.0023 m/s

Fig. Shows the Velocity plot for Case:1 Re=100, v = 0.023 m/s

Fig. Shows the Velocity plot for Case : 1 Re = 100, v = 0.23 m/s

Velocity Comparison plot for Case:1

Fig. Shows the Comparison of velocity plots for Case:1

Case : 2 (Re =1000)

Cut plot at 85% of pipe length

Cut plot at 90% of pipe length Cut plot at 95% of pipe length

Velocity Plots for Case : 2

Fig. Shows the Velocity plot for Case:2 at Re= 1000 and v=0.0023 m/s

Fig. Shows the Velocity plot for Case:2 at Re= 1000 and v=0.023 m/s

Fig. Shows the Velocity plot for Case:2 at Re= 1000 and v=0.23 m/s

Fig. Shows the Comparison of velocity plots for Case:2

Case : 3 (Re =10000)

Cut plot at 85% of pipe length

Cutplot at 90% of pipe length Cut plot at 95% of pipe length

Velocity Plots for Case:3

Fig. Shows the Velocity plot for Case:3 at Re= 10000 and v=0.0023 m/s

Fig. Shows the Velocity plot for Case:3 at Re= 10000 and v=0.023 m/s

Fig. Shows the Velocity plot for Case:3 at Re= 10000 and v=0.23 m/s

Velocity Comparison plot for Case : 3

Fig. Shows the Comparison of velocity plots for Case:3

Conclusion:

  • We can observe from the above plots that for Case:1 the velocity profile is parabolic in nature.
  • The flow is laminar in Case:1 and in Case:2) as the Reynold’s number is lower in both the cases (i.e., Case:1 = 100 and Case:2 = 1000)
  • As the Reynold’s number is high Re= 10000 so the flow is turbulent, the Velocity plot of Case:3 at different velocities not parabolic.
  • We can finally conclude that as the Reynold’s number increases, the flow changes from laminar to turbulent.
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