Page 460 - Handbook of Energy Engineering Calculations
P. 460
Shellside, Eq. (8):
Tube wall, Eq. (11):
Fouling, Eq. (13):
Sum of the Products (SOP):
SOP = 0.191 + 0.235 + 0.250 + 0.039 = 0.715
The assumed exchanger is adequate with regard to heat transfer. The next
step is to check both sides for pressure drop.
4. Make the pressure-drop computation
Tubeside, Eq. (14):
Shellside, Eq. (22):
