Local heat transfer from single tubes in an industrial-sized, three-pass he
at exchanger of the inline tube bundle type was measured. The transversal a
nd longitudinal pitches were 1.80 and 1.5D, respectively, the height of eac
h pass was 30D and the Reynolds number was 20 000. The measurements were ma
de using an electrically heated cylindrical probe of the metallic film type
, an instrument normally used in small-scale laboratory setups to gain deta
iled information about local heat transfer. The probe was positioned at var
ious tube locations and rotated to yield the circumferential variation of t
he local heat transfer. Depending on location, local mean heat transfer was
less than half or more than twice the nominal mean value. These variations
were related to the non-uniform flow distributions present inside the heat
exchanger, evidenced by computational fluid dynamics calculations. Also. t
he calculated velocities were used with an empirical correlation for the Nu
sselt number, and the results agreed very well with the measured values. (C
) 2001 Elsevier Science Ltd. All rights reserved.