Hello,
In an attempt to design a shell & tube heat exchanger using Aspen EDR, I have designed a BHM exchanger to cool syngas from 46 DegC to 18.35 DegC using chilled water at 7 degC with excess area value of 0 %. However, when I used the same exchanger geometry generated by design mode in simulation mode for same flows and inlet temperatures of Syngas & Chilled Water as design case the resultant heat duty is different than that of design mode.
Anybody can highlight what is the reason behind this difference of duty
Said