A proposed technique for controlling jet impingement boiling heat transfer involves injection of gas into the liquid jet. This paper reports results from an experimental study of boiling heat transfer during quenching of a cylindrical 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 bubbles 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 form of boiling curves, maximum heat fluxes, and minimum film boiling temperatures 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-only velocities between 2.0 and 4.0 m/s 11,300Red,fo22,600, several significant effects are associated with introduction of the gas bubbles into the jet. As well as enhancing single-phase convective heat transfer by up to a factor of 2.1 in the stagnation 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 fraction, while minimum film boiling temperatures increase and film boiling heat transfer decreases with increasing void fraction. A companion paper (Hall et al., 2001) details corresponding results from the single-phase jet.

1.
Viskanta, R. and Incropera, F. P., 1992, “Quenching with Liquid Jet Impingement,” I. Tanasawa and N. Lior, eds., Heat and Mass Transfer in Materials Processing, Hemisphere, New York, pp. 455–476.
2.
Wagstaff, R. B. and Bowles, K. D., 1995, “Practical Low Head Casting (LHC) Mold for Aluminum Ingot Casting,” J. Evans, ed., Proceedings, TMS Light Metals Committee, The Minerals, Metals & Materials Society, Warrendale, PA, pp. 1071–1075.
3.
Fischer, H., Wagstaff, F. E., and Ekenes, J. M., 1989, “Airslip and Turbo Development for Aluminum Sheet Ingot,” Proceedings, Ingot and Continuous Casting Process Technology Seminar for Flat Rolled Products, The Aluminum Association, pp. 417–426.
4.
Serizawa, A., Takahashi, O., Kawara, Z., Komeyama, T., and Michiyoshi, I., 1990, “Heat Transfer Augmentation by Two-Phase Bubbly Flow Impinging Jet with a Confining Wall,” G. Hetsroni, et al., eds., Proceedings, 9th International Heat Transfer Conference, Hemisphere, New York, Vol., 4, pp. 93–98.
5.
Chang, C. T., Kojasoy, G., Landis, F., and Downing, S., 1995, “Confined Single- and Multiple-Jet Impingement Heat Transfer—II. Turbulent Two-Phase Flow,” International journal of Heat and Mass transfer, Vol. 38, pp. 843–851.
6.
Lockhart, R. W., and Martinelli, R. C., 1949, “Proposed Correlation of Data for Isothermal Two-Phase, Two-Component Flow in Pipes,” Chemical Engineering Progress, Vol. 45, pp. 39–48.
7.
Zumbrunnen, D. A. and Balasubramanian, M., 1995, “Convective Heat Transfer Enhancement Due to Gas Injection Into an Impinging Liquid Jet,” ASME Journal of Heat Transfer. Vol. 117, pp. 1011–1017.
8.
Hall
,
D. E.
,
Incropera
,
F. P.
, and
Viskanta
,
R.
,
2001
, “
Jet Impingement Boiling From a Circular Free-Surface Jet During Quenching: 1—Single-Phase Jet
,”
ASME J. Heat Transfer
,
123
, pp.
901
910
.
9.
Bar-Cohen, A. and Simon, T. W., 1988, “Wall Superheat Excursions in the Boiling Incipience of Dielectric Fluids,” Heat Transfer Engineering, Vol. 9, pp. 19–31.
10.
Webb, B. W. and Ma, C.-F., 1995, “Single-Phase Liquid Jet Impingement Heat Transfer,” J. P. Hartnett and T. F. Irvine, eds., Advances in Heat Transfer, Academic Press, New York, Vol. 26, pp. 105–217.
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