Page 411 - Handbook of Energy Engineering Calculations
P. 411
and-tube heat exchangers. Figure 4 simplifies the computation of the
uncorrected LMTD for temperature differences ranging from 1 to 1000°F
(−17 to 537.8°C). It gives LMTD with sufficient accuracy for all normal
industrial and commercial heat-exchanger applications. Correction-factor
charts for three shell passes, six or more tube passes, four shell passes, and
eight or more tube passes are published in the Standards of the Tubular
Exchanger Manufacturers Association.