This paper describes experimental efforts aimed at examining the effect of
vapor bubble sliding on forced convection boiling heat transfer. Flow boili
ng experiments using FC-87 were conducted for vertical upflow and downflow
configurations. Both slightly subcooled single-phase and saturated annular
flow boiling were considered. Significantly higher heat transfer rates were
measured for vertical upflow than for downflow with the same wall superhea
t and slightly subcooled single-phase inlet conditions. This increase in he
at transfer is directly attributable to sliding vapor bubbles, which remain
attached to the wall during upflow and lift off the wall during downflow D
ifferences in the measured upflow and downflow heat transfer rates are not
as significant for annular flow boiling, which is due in part to the simila
r vapor bubble dynamics which have been observed for upflow and downflow. H
eat transfer experiments in single-phase subcooled upflow with air bubble i
njection at the heating surface suggest that sliding bubbles enhance the bu
lk liquid turbulence at the wall, which contributes significantly to the ma
croscale heat transfer: It is concluded from this work that vapor bubble sl
iding heat transport can be a significant heat transfer mechanism, and shou
ld be considered in the development of mechanistic flow boiling heat transf
er models.