Up to 2 1 of metastable propane, butane, refrigerant R-134a and water were
released from glass receptacles without nucleation sites and expanded to at
mospheric pressure over a range of initial superheats created by the sudden
depressurization. Above a certain superheat threshold, vaporization occurr
ed only in a thin surface zone of intense boiling and liquid fragmentation.
This boiling front traveled from the free surface into the bulk of the sup
erheated liquid and ejected a high-velocity vapor/liquid stream. For pipe s
izes in the range from 14 to 80 mm, no significant influence of the cross-s
ectional area on the front velocity was noted. The complex interaction of v
aporization and fragmentation of the superheated liquid at the boiling fron
t appeared as a self-amplifying process, as also noted by others. Below a c
ertain superheat threshold, there was no front propagation, and the vaporiz
ation could not carry away surplus liquid. The two-phase flow created at th
e boiling front had a velocity significantly lower than that expected from
isentropic phase change. The pressure created by the acceleration of the tw
o-phase mixture reduces the superheat in the liquid and attenuates the phen
omena, as experiments with orifices have shown. An extensive non-dimensiona
l analysis of the data was conducted. The threshold for boiling front creat
ion and the front velocity were correlated in terms of the relevant thermop
hysical properties and the superheat; the data of other investigators agree
d well with the proposed new correlations. (C) 2001 Elsevier Science Ltd. A
ll rights reserved.