In: Chemistry
Estimate the footprint for a shell-and-tube heat exchanger from the following design data:
Area = 145 m
Hot side temperatures: in at 300°C, out at 195°C
Cold side temperatures: bfw at 105°C, mps at 184°C
Use 12 ft, 1-in OD tubes on a 1-1/4-in square pitch, use a single shell-and tube pass because of change of phase on shell side
Use a vapor space above boiling liquid = 3 times liquid volume
HT area of 1 tube = πDL = π(1/12)(12ft) = 3.142ft2
Number of tubes = (145m2)(3.2808ft/m)2(1/3.142ft2) = 497 tubes
Fractional area of the tubes = π/4(1/1.25)2 = 0.5027
CSASHELL = (4)(777) = 3108in2 ⇒ π/4D2SHELL = 3108in2
DSHELL = √(4)(3108in2)/π = 62.9in = 1.598m
Length of Heat Exchanger (2 + 12 + 2)ft = 16ft = 4.877m
Foot Print = 1.598 × 4.877m