Hi,
I currently designing a C3 distillation column for my design project, however it is not pure propane-propylene, and has H2, C1, C2s etc.
I was wondering what was the best way to calculate the K-Values and thus the relative volatilities of the system? I am working at 16 bar and 40C.
Is there any point taking the H2, C1 and C2s into account when designing the column, or should I just take into account of them when designing the condenser?
Thanks for any help given
Regards