This work is a continuation of a major study performed by the authors
to understand the mechanism of boiling heat transfer in structured boi
ling surfaces. The tests were performed on a tubular surface composed
of an integral-fin tube [1575 fins/m (40 fins/in.) and 0.8 mm fin heig
ht] having a copper foil wrapped over the fin tips. Pores of known dia
meter and pitch are pierced in the foil cover. The resulting surface i
s similar to the Hitachi Thermoexcel-E tube. The tests were conducted
using R-123 at 26.7 degrees C on foil covers having 0.18 or 0.23 mm po
re diameter and 0.75 or 1.5 mm pore pitch. The present study reports b
ubble dynamics data (bubble diameter. bubble frequency and nucleation
site density). The data were obtained using a high speed video camera
at 30 x magnification, The bubble growth mechanism on the enhanced sur
face is different from that on plain surfaces. A significant fraction
of the vaporization occurs at menisci in the corners of the tunnels. T
his evaporation process controls the bubble frequency and nucleation s
ite density. Further, evaporation and bubble growth occur after the bu
bbles emerge from the surface pores. Smaller bubbles are generated on
the enhanced surface and at a greater frequency than on a plain surfac
e for the same heat flux. The enhanced surface has a greater nucleatio
n site density than on a plain surface. (C) 1998 Elsevier Science Inc.
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