Challenge

Week 6: Conjugate Heat Transfer Simulation

Conjugate Heat Transfer Simulation

Aim:

Baseline configuration

  • Setup a flow simulation through a pipe
  • Inlet Reynolds number should be 7,000
  • Turbulence modelling - K-Epsilon
  • Supercycling parameters - same as in the video

Grid dependence test

  • Start with an initial base grid
  • Run grid dependence test on 3 grids and show that the outlet temperature converges to a particular value

Effect of supercycle stage interval

  • Set supercyle stage interval to 0.01,0.02 and 0.03
  • For these three values, how does the total simulation time compare against the baseline configuration

Geometry:

The geometry was imported into the converge and Cad clean up was done.

  • inner radius = 0.015
  • outer radius = 0.02
  • length = 0.2

Case-Setup

  • Application: General Flow
  • Solver: Steady state solver
  • Material: Air
  • Solid - Aluminium
  • Species: O2 and N2
  • Simulation mode: Full hydrodynamic
  • Simulation time parameters:
    Start time:0sec
    End time:0.5 sec
  • Region & Initialization:
    Created a fluid and solid region for initializing the setup

Boundary conditions

  • Inlet:
  • Boundary type = inflow
  • Pressure = zero gradient (Neumann boundary condition)
  • Temperature = 300 K
  • Velocity = 7.2877 m/s
  • outlet:
  • Boundary type = outflow
  • Pressure = 101325 Pa
  • Temperature = 300 K
  • Species = air
  • Solid outer wall
  • Boundary type = wall with slip condition
  • Wall motion type = stationary
  • Temperature = -10000 w/m2 (Heat flux)
  • Solid side
  • Boundary type = wall with slip condition
  • Wall motion type = stationary
  • Temperature = zero gradient (Neumann boundary condition)
  • Interface
  • Boundary type = interface
  • Boundary type = interface
  • region 1 = Fluid region
  • Stream ID = 0
  • Temperature = 300 K
  • Pressure = 101325 Pa
  • Species = air
  • region 2 = Solid region
  • Stream ID = 1
  • Temperature = 300 K
  • Solid option - enabled
  • Species = Aluminium
  • Boundary type = interface
  • region 1 = Fluid region
  • Stream ID = 0
  • Temperature = 300 K
  • Pressure = 101325 Pa
  • Species = air
  • region 2 = Solid region
  • Stream ID = 1
  • Temperature = 300 K
  • Solid option - enabled
  • Species = Aluminium
  • Turbulence Model - K epsilon
  • The time interval for writing 3D output data files:=0.01
  • The time interval for writing text output:1e-6 sec
  • The time interval for writing restarting output:0.01
  • Maximum number of restart file saved:3
  • Super cycling
  • Time length for cycle stage = 0.01, 0.02, 0.03.

Results

  • Mesh

1. mesh size 0.004

2. mesh size 0.003

3. mesh size 0.002

4. mesh size 0.001

  • Velocity Contours

1. mesh size 0.004

2. mesh size 0.003

3. mesh size 0.002

4. mesh size 0.001

  • Temperature

1. mesh size 0.004

2. mesh size 0.003

3. mesh size 0.002

4. mesh size 0.001

  • Pressure

1. mesh size 0.004

2. mesh size 0.003

3. mesh size 0.002

4. mesh size 0.001

  • Wall Y+

1. mesh size 0.003

2. mesh size 0.002

3. mesh size 0.001

  • Temperature Plots with mesh refinement

  • Temperature plots with super-cycle time length variation (mesh = 0.02)

.

Conclusion

  • CHT analysis is done on solid-hollow cylindrical geometry.
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