2006
DOI: 10.1134/s1531869906010096
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Heat transfer and crisis phenomena with intense boiling in the falling wave liquid films

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2006
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Cited by 22 publications
(20 citation statements)
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“…As can be seen from the diagram, there are two areas with different rates of a change in the vapor front velocity, depending on the temperature rise. In the area of low overheating, the growth rate of the front velocity vs. wall superheat is satisfactorily described through the calculation by the model [5]. In the area of high overheating, the significantly higher growth rate of the front velocity vs. wall overheating is observed.…”
Section: Resultsmentioning
confidence: 57%
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“…As can be seen from the diagram, there are two areas with different rates of a change in the vapor front velocity, depending on the temperature rise. In the area of low overheating, the growth rate of the front velocity vs. wall superheat is satisfactorily described through the calculation by the model [5]. In the area of high overheating, the significantly higher growth rate of the front velocity vs. wall overheating is observed.…”
Section: Resultsmentioning
confidence: 57%
“…Usual water and organic, cryogenic liquids, and liquid mixtures and solutions are usually used as the working liquids [3,4]. Limiting the intensity of heat removal is caused by formation of a vapor film near the heat transfer surface and, in particular, it is determined by the dynamics of this film propagation along the heating surface [5,6].…”
Section: Introductionmentioning
confidence: 99%
“…The stronger dependence of the front velocity wall on wall overheating in the area of ΔT > 60 K indicates the intensification of evaporation at the interface. In [7] this intensification of evaporation is explained by development of Landau instability [9]. Considerable variation of instantaneous velocity at the constant values of wall overheating relates to pulsations of interface velocity.…”
Section: Resultsmentioning
confidence: 99%
“…This effect can be shown both in the systems of film and droplet irrigation [1][2][3], and under the conditions of a large volume [4]. There are a number of models describing distribution of the self-sustained undisturbed evaporation front [5,6], as well as the single attempts to model the dynamics of front propagation with consideration of small-scale interface perturbations the under conditions of intense evaporation [7].…”
Section: Introductionmentioning
confidence: 99%
“…Models proposed previously [1,[5][6][7][8][9] aimed at approximate description of the dependence of evaporation front propagation velocity on some set of physical parameters. Some of these models [5,7,9] suggest that a "frontal stagnation point" exists at the interface. However, some recent experimental data did not confirm the existence of the frontal stagnation point [2], which implies the need for developing a new approach to the description of these phenomena.…”
Section: Introductionmentioning
confidence: 99%