By S. G. Kandlikar
Offers a complete insurance of the elemental phenomena. It includes twenty-five chapters which hide assorted points of boiling and condensation. First the explicit subject or phenomenon is defined, via a short survey of past paintings, a phenomenological version in keeping with present realizing, and eventually a collection of prompt layout equations or correlations. distinct references are indexed on the finish of every bankruptcy for extra interpreting.
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M. keio. uk Ramesh K. jp Vijayaraghavan Srinivasan Praxair Inc. jp Yoshio Utaka Dept. of Mechanical Engineering & Materials Science, Faculty of Engineering. jp Larry C. edu Akira Yabe Mechanical Engineering Department AIST, Min. Int. jp CHAPTER ONE VAPOR LIQUID EQUILIBRIUM PROPERTIES Yasunobu Fujita Kyushu University, Hakozaki, Fukuoka 812-8581, Japan Satish G. Kandlikar Rochester Institute o/ Technology, Rochester, NY 14623, USA The analysis of phase change heat transfer between liquid and vapor or the design of an evaporator or a condenser requires an understanding of the principles of two phase equilibrium and an application of equilibrium data.
T (2); P - Pg, (9); ( 1 3); ( 1 7), (6); (7. 2) ; ( 1 9. 1 -44) ( 1 9. 4) NOMENCLATURE xxxv boundary oflayermassthickness ofboundary liquid layer, m thickness diffusion 8/8\ in initial macrolayer thickness, m, of Lennard-Jones po phase fraction; energy parameter tential, emissivity, dielectric void fraction, constant of vapor, 2/s, eddy diffusivity, m absolute electrical permi ttivity, (F/m), homogeneous void fraction, 2/s, eddy diffusivity for heat, m correction factorparameter for effectthatof subcooling onderCHF,Pol Equa dimensionless controls van tion,o of maximum angle measured from stagnation point, rati flow area, dynamic viscosity, kglm s; similarity variable, fin efficiency, enlargement ratio fortheheatrelatitransfer area, dynamic contact vari a ble expressing o n between angle and contact angle,dimensionless angle of channel inclinationcontact from hori zontal, temperature, an gle, angle, radial acceleration, angle to vertical measured from top of tube, fin half-tip angle, Time interval, angle, advancing contactangle, angle,rad,rad, retreati n g contact critical c contact angle, i.
It is generally known that the specific volume of liquid can be increased along line Be; thus, it is possible to superheat the liquid above the saturation temper ature in the absence of vapor nucleation. Similarly, the specific volume of vapor can be decreased along line F E, making it possible to subcool the vapor below the saturation temperature in the absence of droplet nucleation. The superheated p A \ {im: :: �; : {';:;C-- sPinOdal-- ----\ �j;X :i . ",... : / , . G .. Figure 3 V Superheating of liquid, subcooling of vapor, and an isotherm predicted from the van der Waals equation of state.
