Hi,
I have to design a heat exchanger that evaporates Propane and condensates propylene but I tried using a kettle rebiller but the area required is so immense I'm very unsure it's correct.
m_propane = 25 kg/s
latent heat propane = h_propane_liquid - h_propane_vapour = 279.81 kJ/kg
U_ass = 200 W/m2C
T_m = | T_propane-T_propylene | = 7.7
A = (latent heat propane*m_propane)/(U_ass*T_m) = 4534 m2
Is this anywhere near correct?
Attached Files
Edited by dwsv, 06 March 2017 - 05:42 PM.