Ht. Liu et al., CHARACTERISTICS OF TRANSITION BOILING AND THERMAL OSCILLATION IN AN UPFLOW CONVECTIVE BOILING SYSTEM, Experimental thermal and fluid science, 8(3), 1994, pp. 195-205
The characteristics of transition boiling and thermal oscillation in a
single-channel forced-convection upflow system were experimentally st
udied. The working fluid, R-12, flows vertically upward inside the tes
t channel of inside diameter 2.85 cm and outside diameter 3.37 cm. The
test section is 339 cm long and is heated by the Joule effect. Temper
ature fluctuations were measured in the tube wall in the transition bo
iling region under both hydrodynamically stable and unstable condition
s. Without exit restriction, the system was hydrodynamically stable, a
nd the usual irregular wall temperature fluctuation in the transition
boiling region was observed; with an exit restriction, the system was
found to be hydrodynamically unstable, and sustained temperature fluct
uations with greater magnitudes and much larger periods were observed.
Wall temperature fluctuations of this type are termed thermal oscilla
tion. During thermal oscillation the hydrodynamic instabilities were a
lso measured. The system pressure oscillations were measured at the in
let and the void fraction oscillations were measured at the exit with
a capacitance void meter. The mechanism of thermal oscillation is give
n, and the effects of heater wall capacitance and axial conduction on
the processes of transition boiling and thermal oscillations are studi
ed. Typical graphs of instantaneous heat flux to the fluid versus time
as well as typical recordings of wall temperature oscillations are pr
esented. The instantaneous heat flux to the fluid versus the wall temp
erature is also plotted, and a limit cycle is produced. The critical h
eat flux (CHF) values were determined under both hydrodynamically stab
le and unstable conditions and are compared on maps of CHF versus exit
quality at different mass fluxes with constant system pressure. This
study shows that the hydrodynamically unstable system has substantiall
y lower CHF values. Thermal oscillation has been observed over the fol
lowing parameter ranges: mass flux, 300-3000 kg/(m2 s); heat flux, 25-
80 kW/m2; inlet quality, -0.2 to +0.6; system pressure, 10 bar.