Hello,
I have been currently tasked with designing a total overhead condenser for a methanol distillation column. In the condenser, for simplicity reason, have I said that a pure vapour methanol product enters the condenser. From the sources, I have concluded that the best action would be a shell and tube, which is horizontal, and the condensation takes place on the shell side. From this, I will also have cooling water running through the tube side. From the literature studied, I cannot find an equipment sizing procedure to work out the overall heat coefficient, which is then used to work out the transfer heat area for the heat exchanger stated, so I wondered if anyone has any guidance or references that can help me through it. I have access to simulation on ChemCAD in where I can obtain any physical properties.
I would use `Engineering Sciences Data Unit Design Guide, ESDU 84023`, but I don't have access to it, neither does my university, which is proposed in Coulson and Richardson.
Heat Exchanger Type: Shell and Tube
Orientation: Horizontal
Condensation occurs in the Shell Side
Totally condensed
Hot stream: Pure Methanol
Cold Stream Cooling Water
Thanks
David.S.J