Tube-to-tube heat transfer is suspected to affect the overall capacity of m
ost finned-tube heat exchangers running subcooled (single-phase) simple sub
stances, or zeotropic mixtures, as coolants. A simplified numerical model i
s presented and used for simulating the heat transfer process of air flowin
g in between two parallel fins of a finned-tube heat exchanger with known t
ube temperatures. The objective of the numerical simulation is to detect th
e existence of tube-to-tube heat transfer and the corresponding detrimental
impact it might have on the overall capacity of the heat exchanger. The nu
merical simulation considers a 4 x 3 finned-tube, single-phase, air-water h
eat exchanger with data provided by the National Institute of Standards and
Technology (NIST). Results indicate the existence of strong tube-to-tube h
eat transfer along the fins (particularly among neighboring tubes presentin
g very different temperatures, as expected). The tube-to-tube heat transfer
phenomenon is shown to account for approximately 20% of the heat exchanger
capacity. Thin adiabatic layers placed along the fin surface are shown, al
so through numerical simulations, to be very effective in interrupting the
tube-to-tube heat transfer phenomenon. A simplified analytical procedure to
estimate the tube-to-tube heat transfer effect of any finned-tube heat exc
hanger, suggested as a design tool, is satisfactorily tested against the nu
merical results.