Divergence on RPI Model
Dear all,
I am modeling nucleate boiling on FLuent using the RPI model. I can detect the vapor phase after some iterations (using steady state) but after that the calculation diverges (normally: turbulent viscosity limited to viscosity ratio 1e+5). Also, using axisimmetric the vapor phase appears before the saturation temperature (30K before) and the divergence occurs only when Tsat is achieved). There's a lot of correlations to phase iteration but I am following some papers. Does anybody have any idea of how to solve this? I tryed to reduce relaxation factors, change my mesh, 2D and 3D geometries, solution methods (it is more sateble with SIMPLE Presure-Velocity coupling, but everybody says to use Coupled, so I am trying). Thaks! |
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