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[TRNSYS-users] pb convergence with type 60
Hello,
I can't find a good
way using type 60 in yearly simulation : to run until the end because
of non convergence pb on heat exchanger's UA calculation : no problem when I use
small flow rate (280L/h) and small tube's diameters (around 15mm) but no way if
I try to run simulation with 280 L/h of flow rate and heat exchanger tube
diameter around 30mm.
I do not use glycol
as fluid , just water.
The timestep is
small (10s) and I tried to increase internal timestep , number of derivatives
with no significant improvement.
I thought it
was improved in TRNSYS 16 but I can't find the solution.
Has anyone
encountered (and solved) this problem ?
Thanks
David
Chèze
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