Heat-transfer coefficients in film boiling

Bankoff [343] suggested that heat transfer coefficients in film boiling could be substantially improved by continuously removing vapor through a porous heated surface. Subsequent experimental work [344, 345] demonstrated that coefficients could be increased by as much as 150 percent, provided that a porous block was placed on the surface to stabilize the flow of liquid toward the surface. Wayner and Kestin [346] extended this concept to nucleate boiling and found that wall superheats could be maintained at about 3 K (5.4°F) for heat fluxes over 300,000 W/m2 or 95 x 103 Btu/(h-ft2). This work was extended by Raiff and Wayner [347], The need for a porous heated surface and a flow control element appears to limit the application of suction boiling. 

FIGURE 15.71 Heat transfer coefficient in film boiling of water from a 3-mm-diameter cylinder (from Sakurai and Shiotsu [180], with permission from Taylor Francis, Washington, DC. All rights reserved). 

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