TECHNICAL PAPERS: Boiling and Condensation

Jet Impingement Boiling From a Circular Free-Surface Jet During Quenching: Part 2—Two-Phase Jet

[+] Author and Article Information
David E. Hall

Michelin Americas Research Corporation, 515 Michelin Road, Greenville, SC 29602

Frank P. Incropera

Notre Dame University, South Bend, IN 46556e-mail: fpi@nd.edu

Raymond Viskanta

School of Mechanical Engineering, Purdue University, West Lafayette, IN 47907

J. Heat Transfer 123(5), 911-917 (Mar 22, 2001) (7 pages) doi:10.1115/1.1389062 History: Received May 27, 1997; Revised March 22, 2001
Copyright © 2001 by ASME
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Schematic of two-phase nozzle and boiling on the test surface
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Dependence of static head on void fraction for selected liquid-only velocities
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Jet impingement following initiation of quench (t=2 s) for for=0.0, 0.1, 0.2, and 0.3 (Ti=650°C,Vfo=3.0 m/s,ΔTSUB=75°C)
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Bubble size distribution for various void fractions (Vfo=3.0, s. Red,fp=17,000)
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Effect of void fraction on the boiling curves for r=0, 10, 20, 30, and 40 mm (Ti=650°C,Vfo=3.0 m/s,ΔTSUB=75°C)
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Effect of void fraction on the stagnation point boiling curve (Ti=650°C,Vfo=3.0 m/s,ΔTSUB=75°C)
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Effect of void fraction on the boiling curve for r=20 mm (Ti=650°C,Vfo=3.0 m/s,ΔTSUB=75°C)
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Minimum film boiling temperature distribution (Ti=650°C,Vfo=3.0 m/s,ΔTSUB=75°C)
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Variation of maximum heat flux with position, ∝, and Vfo (Ti=650°C,ΔTSUB=75°C)
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Variation of single-phase heat transfer Nusselt numbers with Vfo and ∝




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