Enhancement of heat transfer due to slug bubbles passing through a capillar
y channel submerged into liquid is considered. A model of hydrodynamics is
proposed describing the influence of the entrance region of the rectangular
channel, Different regimes of heat transfer depending on fourth time-value
s of process: tau(0), t(c) = L-c/U-b, t* = y*/U-l, t(b) = V/(UbS) are deter
mined. A physical model of heat transfer takes to account the influence of
liquid velocity, nonstationary effect of bubbles passing near heater and pr
edominantly influence of the thermal layer forming on the low part of the h
eater. The calculation from this model is shown to provide agreement with e
xperimental data.