Hello,

I am trying to simulate a gas stirred vessel using Eulerian model in Fluent. However, I have a diveregence in epsilon.

The turbulent intensity and hydraulic diameter conditions for turbulence inlet are used and outflow condition is used for outlet. Mesh consists in a 21,000 elements with orthogonality 100%. Mesh near to plume and interphase region is refined. I have to say that I used same parameters for a scale model (1/17) and successfully runs.

Thank you for you comments.

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