My problem is not simple (for me at least). To make it easier, let's say it's a heat exchanger which I need to simulate and rate. I've got all old data for it but my problem is I cannot make it converge...
The hot fluid runs through tubes (H2 ~ 75%, C1 ~ 12%, G.O ~ 5,8% and others in volume) at 242ºC, 9930 KPa while the cold fluid runs through shell (Diesel, Kerosene, Hvy. Naphtha, Light Naphtha, unconverted gasoil, H2 etc) at 74ºC, 11400 KPa. Both streams exchange heat, condense and evaporate at the same time. I made the simulation but HTFS-TASC keeps telling me it has errors because it wasn't given the dynamic viscosity of the inlet streams (obviously, this is because both streams are non-homogenous)so I can't rate it. I also did some other simulations but with simpler fluids (for my problem I used their distillation curves, but for the latter I used 4 fluids which mixed gave a vapor/liquid mix like my earlier problem)
and they all converged... why my problem can't???
HELP!
I've attached a hysys 2006 simulation file.