Jet impingement boiling from a circular free-surface jet during quenching:Part 2 - Two-phase jet

A proposed technique for controlling jet impingement boiling heat transfer involves injection of gas into the liquid jet. This paper reports results f rom an experimental study of boiling heat transfer during quenching of a cy lindrical copper specimen, initially at a uniform temperature exceeding the temperature corresponding to maximum heat flux, by a two-phase (water-air) , circular, free-surface jet. The second phase is introduced as small bubbl es into the jet upstream of the nozzle exit. Data are presented for single- phase convective heat transfer at the stagnation point, as well as in the f orm of boiling curves, maximum heat fluxes, and minimum film boiling temper atures at locations extending from the stagnation point to a radius of ten nozzle diameters. For void fractions ranging from 0.0 to 0.4 and liquid-onl y velocities between 2.0 and 4.0 m/s (11,300 less than or equal to Re-d,(fo )less than or equal to 22,600), several significant effects are associated with introduction of the gas bubbles into the jet. As well as enhancing sin gle-phase convective heat transfer by up to a factor of 2.1 in the stagnati on region, addition of the bubbles increases the wall superheat in nucleate boiling and eliminates the temperature excursion associated with cessation of boiling. The maximum heat flux is unaffected by changes in the void fra ction, while minimum film boiling temperatures increase and film boiling he at transfer decreases with increasing void fraction. A companion paper (Hal l et al., 2001) details corresponding results from the single-phase jet.