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Heat exchange pipe with a helical vortex promoter: what is causing divergence? |
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May 8, 2018, 04:37 |
Heat exchange pipe with a helical vortex promoter: what is causing divergence?
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New Member
Haneen JH
Join Date: Apr 2018
Posts: 1
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Hello,
I have been trying to run a 3D model representing the evaporation in a heat pipe with a return line inside the pipe. The suggestion to create a vortex promoter was to add a helical spring in the pipe. Experimentally heat extracted from the pipe with the spring was higher than without the spring. Now computationally, the solution always diverges!! I will list the steps I followed and would appreciate it if you can point out a possible error. Meshing: The pipe is 23 mm long, elements reached 1 mill, and want to limit it to that since my computer is not super! However, metrics are good. Model setup: - Multiphysics, Eulerian evaporation-condensation model/ I also tried Boiling model -Viscosity, k-eps, Lee, Implicit / I also tried k-omega Boundary conditions: -Inner wall Temp 103 degrees(saturation) -Outer wall Temp 300 degrees -Pressure Inlet 13 kPa -Pressure Outlet 11 kPa Solution trials: - simple -coupled courant 0.9, 1, 5, default 200 -coupled pseudo transient URF reduced -initialization both hybrid and standard and the list of attempts goes on! I attache the geometry which I really think might be a problem Any suggestions? Thanks in advance |
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Tags |
complex geometry, eulerian multiphase, evaporation condensation, heat pipe |
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