I am trying to solve my model of heat exchanger with finned tubes in Fluent. First variant with air velocity of 1 m/s converged after cca 550 iteration in k-epsilon model. Now I choose velocity of 2 m/s and program refer divergence. After that i try another model (Reynolds stress, and was same. Now choose k-omega standard model and as you can see programm working but probably convergence will not occuar. What to do to obtain better convergence?

Mesh model have 8 million elements and 12 inflating layers on air side?  

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