Heat Exchanger Calculations
Two basic formulas are used in all heat exchanger calculations. These are:
Heat transfer Btu/hr = lbs/hr x sp ht x temp. change °F
In the case of water, the specific heat can usually be considered as 1.0 and
the formula expressed as:
Btu/hr = flow rate in GPM x 500 x temp. change °F (1)
where:
500 = 8.33 lbs/gal x 60 min/hr conversion to lbs/hr
Heat transfer in Btu/hr = (U)(A)(LMTD) (2)
where:
U = overall heat transfer coefficient
A = heat transfer area in sq. ft.
LMTD = log mean temperature difference
= (large temp. diff.) - (small temp. diff.)
all divided by:
the natural log of (large temp. diff - small temp. diff)
The range of the heat transfer coefficient "U" varies widely, depending upon
the physical conditions involved, such as the solution viscosities, surface
fouling, fluid velocities and turbulence, constant or change of state, and metal
resistance.
For example, water-to-water heat exchangers typically have "U" value ranges
like:
Plate-frame: 500 to 1,200 Btu/(hr x sq ft x°F)
Shell and tube: 150 to 350 Btu/(hr x sq ft x°F)
Plate-coil: 50 to 250 Btu/(hr x sq ft x°F)
These can be contrasted to "U" values of 4 to 8 for air-to-air or steam-to-air
heat transfer, which is why these are usually plate-fin coils with very large
surface areas.