Hi,


Short brief

I am trying to design a partial condenser for de-ethanizer..
the condenser is a shell and tube...

Shell side = Hot stream = partial condensation
Tube Side = cold side = Gas and no phase change along the exchanger

Stream components are C1,C2,C3,C4,H2,He,N2 for shell and tube side


All material balance across the exchanger / distillation has been calculated using Hysys..


Wondering if any1 has any documents or examples I can have a look at for partial condensers,,

I know how 2 design normal shell and tubes using Kern method without phase change, also I had a look and total condensers but not partial condensers.

Regards