Third heat transfer crisis at subcooling

The effect of liquid subcooling below the saturation temperature on the third heat transfer crisis was studied experimentally at pool boiling. Experimental data on the threshold values of superheating and heat fluxes, above which the evaporation front and third heat transfer crisis for acetone at subcooling from 0.3 to 10 K are formed, were shown. Formation of evaporation fronts is the necessary, but not sufficient condition for the third heat transfer crisis at subcooling. It was found that formation of a stable vapor film after propagation of condensation fronts over the heater surface is possible at heat fluxes considerably lower than the first critical one.     

Interconnection between dynamics of liquid boiling-up and heat transfer crisis for nonstationary heat release

This paper deals with investigation results on crisis phenomena for nonstationary heat release under the conditions of free convection and in falling liquid films. It is shown that the character of the crisis development and the critical heat flux for nonstationary heat release significantly depend on the characteristics determining the temperature head of liquid boiling-up. According to experimental data with an arbitrary temporal function of heating, the character of the dependence between the critical heat flux and the heat release increasing rate is significantly effected by ready nucleation sites. It is found that a change in the nonstationary critical heat flux in the range of high times between impulses for periodic heat release is connected with deactivation of ready nucleation sites on the heat-releasing surface. According to new experimental results, in the studied range of irrigation degree alteration (Re_in = 30–1660), parameters characterizing decay of the falling liquid film with stepped heat release (the distribution of the time of boiling-up expectation along the liquid film, the velocities of movable boundaries in the boiling-up and drying fronts, the intensity of liquid ejection from the heat-releasing surface) complexly depend on the Reynolds number, wave characteristics, and heat flux density. The text was submitted by the authors in English.     

Dynamics of explosive boiling and third heat transfer crisis at subcooling on a vertical surface

Results of experimental studies on dynamics of explosive boiling and third heat transfer crisis under the conditions of liquid subcooling are presented for the vertical arrangement of the heat-transfer surface. Acetone was used in experiments at the pressure in the working volume from 20 to 46 kPa and subcooling from 0 to 20 K. The studied processes were recorded. Data on the velocity of evaporation front propagation at liquid subcooling were obtained. These data are compared with the results of calculations according to the models available in the literature. The effect of liquid subcooling on the regions of regime parameters corresponding to explosive boiling and third heat transfer crisis is studied.     

Investigation of transient processes at liquid boiling under nonstationary heat generation conditions

The paper presents results on experimentally investigated dynamics of boiling development and formation of film boiling zones under stepwise heat generation on a horizontally and vertically oriented cylindrical surface in a large volume of Freon-21. Experimental data on the expectation time and boiling temperature, the propagation velocity and structure of evaporation and boiling fronts for different heat flux density both in saturated liquid and in subcooling conditions are obtained. Results of experiments on investigating the nucleation forms under development of nonstationary heat release crisis caused by heat loading on the vertical heater immersed into the volume of liquid (water, ethanol) subcooled to saturation temperature are presented. A calculation ratio for determining the expectation time to the beginning of intense vaporization in water is proposed and compared with experimental data obtained on surfaces with different-size roughness. Peculiarities of evolution of evaporation fronts from incipient bubbles are investigated in the experiments with ethanol. Data on the evaporation front velocity as a function of wall overheating are obtained. The obtained experimental data on the propagation velocity of self-sustained evaporation fronts are compared with the known calculated data.     

Dynamics of transient processes at liquid boiling-up in the conditions of free convection and forced flow in a channel under nonstationary heat release

Results on experimental investigation of the dynamics of boiling-up at stepwise heat release on a horizontally oriented cylindrical surface in a large volume of freon-21 are presented. Experimental data on the propagation velocity, structure, and other local characteristics of development of self-sustained evaporation fronts at different temperature differences of boiling-up in saturated liquid were obtained. New experimental results on the dynamics of vapor phase incipience and evolution on the surface of a vertical heat releasing tube and on the dynamics of changing the heater temperature and pressure in a flow of liquid (water, ethanol) subcooled to saturation temperature in the channel under nonstationary heat release conditions are represented. It was revealed that the dependence of the expectation time of intense bubble growth on the water motion velocity is nonmonotonic.     

Heat transfer at evaporation of falling films of Freon mixture on the smooth and structured surfaces

The paper presents the results of experimental investigation of heat transfer and hydrodynamics of falling films of binary mixtures of R21 and R114 freons on the surfaces with complex configuration. The vertical tubes of 50-mm diameter with the smooth and structured surfaces, made of D16T alloy, were used as the working sections. The range of film Reynolds number at the inlet to the working section was Re =10÷155. The image of wave surface of the falling liquid film was visualized and recorded by a high-speed digital video camera. At evaporation the heat transfer coefficients on the smooth and structured surfaces are determined by the liquid flow rate and weakly depend on the heat flux. At low liquid flows, the heat transfer coefficients on the structured surface decrease in comparison with the smooth surface because of liquid accumulation and enlargement of efficient thickness in microtexture channels. At high liquid flows, a change in the structure of the wave film surface leads to an increase in heat transfer coefficients in comparison with the smooth surface.     

蒸发性对燃油瞬态喷雾撞击壁面的动态传热影响

直喷发动机燃油喷雾撞击壁面形成油膜,导致燃烧效率降低,颗粒物排放增加。伴随撞壁的动态传热过程对油膜蒸发具有重要影响。本文针对正戊烷、甲醇、甲醇汽油混合燃料瞬态喷雾撞击壁面,研究了不同条件下蒸发性对燃油瞬态喷雾撞击壁面动态传热影响。结果表明,提高喷油温度可促进燃油雾化,增大喷油压力或降低喷油距离可提高液滴撞壁强度,缩短液膜存在时间。撞壁瞬态温度与热流密度动态变化特征受燃油蒸发性与喷雾条件联合影响。     

Heat transfer and crisis phenomena at boiling in Freon mixture films falling down the structured tube

Investigation results on hydrodynamics, heat transfer, and crisis phenomena in laminar-wave liquid films falling down the surfaces of different geometry are presented in this study. Freon mixture R21/R114 with initial concentration of low-boiling component of 4?C16.6 % was used as the working liquid. The film Reynolds number at the inlet to the experimental section varied from 60 to 700. The heat flux density was changed within 0?C5 W/cm². The images of wave surface of the falling liquid film and formation of dry spots were visualized and recorded by the high-speed video camera. Results of investigation of the wave structure of the film surface, measurements of heat transfer coefficients under the conditions of boiling, and critical heat fluxes in the film flow over the smooth and structured surfaces are presented.     

Heat transfer in boiling of refrigerant R-21 in a downward flow in an assembly of minichannels

The paper presents the results of an experimental study of heat transfer in boiling of refrigerant R-21 in a downward flow in a vertical assembly of minichannels of a plate-fin heat exchanger. Characteristic regimes of vapor-liquid flow and heat transfer coefficients have been obtained for the case of plain fins in the ranges of low mass velocities and heat fluxes that are typical of the industry but poorly studied. The obtained data show no significant dependence of the heat transfer coefficient on the heat flux density and mass velocity, which may be explained by the decisive effect of the evaporation of thin liquid film on the heat transfer at low heat flux density.     

竖直矩形微槽内的特殊干涸与换热行为

利用宽视场体视显微镜、高速摄影仪以及CCD摄像系统对纯蒸发和沸腾换热情形下竖直矩形毛细微槽内液体的特殊干涸行为进行了观察,对液体沿微槽槽道方向的润湿高度进行了观察测量,并对液体沿微槽槽道方向的相变换热特性进行了实验研究.实验结果表明:竖直矩形毛细微槽群是一种高性能的相变换热强化表面,微槽中液体的蒸发与沸腾对干涸点高度的变化有着复杂的影响,热流密度和相变换热系数沿槽道方向的分布不均匀.     

强化管管外升膜蒸发换热特性实验

升膜蒸发是利用微细槽道对液体的毛细抽吸作用,在强化管外表面覆盖一层薄液膜,进而以薄膜蒸发的形式实现强化换热.本文针对强化管在水中的浸入深度,蒸发压力,加热壁面过热度等因素对升膜蒸发换热性能的影响展开实验研究.实验结果表明随着管外液位的降低升膜蒸发换热系数明显提高,此外,蒸发压力和加热壁面过热度因素对升膜蒸发换热性能也有着显著的影响.     

毛细微槽内的相变传热的实验研究

本文对矩形毛细微槽竖直板的相变传热特性进行了实验研究。结果表明毛细微槽对相变换热具有很大的促进作用。当壁面过热度较小时,相变换热形式主要是三相接触线附近的蒸发换热机制。而当过热度较大时,微槽内发生剧烈的沸腾。微槽内相变换热的临界热负荷有两种产生机理:其一是当微槽长度较大时微槽内由于流动阻力而产生的液体输运临界;另一机理是当微槽长度较小时的池内沸腾临界现象,亦即由动态微液层模型决定的临界机理。实验还得到了微槽强化传热的最佳优化尺寸。     

Features of dry spot evolution at the film flow of cryogenic liquids at non-stationary heat release

Transitional processes with dry spot formation and drying crisis development were studied experimentally for the gradual and quasi-stationary laws of heat release on a thin-wall heater cooled by a falling film of cryogenic liquid. It is shown that for low densities of the heat flux, the laminar-wave liquid film decays with formation of a self-organizing system of metastable regular structures with boiling liquid jets and large dry zones between them. The numerical experiment modelling the process of repeated wetting of a superheated surface dried by impulse heat release was carried out. It was found for the first time that the local motion velocities of different zones of the 2D wetting front differ significantly. Reliability of results obtained by numerical methods was proved by direct comparison with experimental data. The work was financially supported by the Russian Foundation for Basic Research (Grant No. 5-08-18022-a) and Siberian Branch of RAS (Integration project of SB RAS together with ITP of UB RAS No. 2.5).     

Experimental Study of the Influence of Structured Capillary-Porous Coatings on the Dynamics of Development of Transient Processes and the Crisis Phenomena at Stepwise Heat Release

The effect of structured plasma-sprayed capillary-porous coatings on transient processes and the development of crisis phenomena at boiling under pulsed heat release was studied. The working fluid was liquid nitrogen on the saturation line at atmospheric pressure. It is shown that under unsteady heat release, there is a degeneration of the development of the boiling crisis on heaters with structured capillary-porous coatings at q < q_CHF (critical heat flux at steady heat release). Under unsteady pulsed heat release, no rapid transition to the film boiling regime (without passing through the nucleate boiling stage) is observed on heaters with such coatings until the thermal load is more than two times higher than the critical heat flux for steady heat release. This significantly increases the times of transition to post-critical heat transfer. Analysis of synchronized measurements of surface temperature of heaters and high-speed video recording of transient processes shows that the degeneration of the heat transfer crisis at q < q_CHF on samples with coatings occurs due to significantly lower liquid boiling temperature differences and specific features of the dynamics of propagation of self-sustaining evaporation fronts in comparison with a smooth heater.     

循环系统中闪蒸换热特性的实验研究

本文针对循环系统中闪蒸的换热特性进行了实验研究,通过可视化系统对闪蒸形态进行了记录和分析,并得出了换热系数与各影响参数之间关系的实验关联式.实验结果表明:当循环水流量为0.028kg/s时,随着过热度的增大,换热系数变化较小,而循环水流量为0.056 kg/s和0.083 kg/s时,换热系数随过热度的增大而减小;同时发现换热系数随水膜厚度的增大而减小.可视化分析表明,闪蒸形态随闪蒸室内饱和压力的减小而变剧烈,闪蒸换热系数随之减小.     

纳米尺度下气泡核化生长的分子动力学研究

采用分子动力学方法模拟纳米尺度下液体在固体壁面上发生核化沸腾的过程,主要研究壁面浸润性对气泡初始核化过程和气泡生长速率的影响以及固-液界面效应在液体核化沸腾的能量传递过程中所起到的作用.研究结果发现：壁面浸润性越强,气泡在固壁处越容易核化.该结果与经典核化理论中“疏水壁面易于产生气泡”的现象产生了明显的区别.其根本原因是在纳米尺度下,固-液界面热阻效应不能被忽略.一方面,在相同的壁温下,通过增强固-液相互作用,可以显著降低界面热阻,使得热量传递效率提高,导致靠近壁面处的流体温度升高,气泡核化等待时间缩短,有利于液体沸腾核化.另一方面,气泡的生长速率随着壁面浸润性的增强而明显升高.当气泡体积生长到一定程度时,会在壁面处形成气膜,从而导致壁面传热性能恶化.因此,通过壁面的热流密度呈现出先增大后减小的规律.     

聚变堆偏滤器过冷水流动沸腾强化换热性能研究

选择欧拉多相流模型和非平衡沸腾模型,用Fluent 软件对单边受热竖直向上平滑管进行了过冷流动沸腾换热的数值分析。研究了不同质量流速、进口温度和热流密度对对流换热系数和空泡份额的影响,并分析了它们对传热恶化的影响。     

微小空间蒸发传热的可视化实验研究

微小结构中蒸发传热过程的研究对高性能传热设备如毛细蒸发器等的设计和性能的提高 有着重要作用,因此成为近年来国内外传热界的研究热点之一。接触角在微小结构蒸发传热过程中 是一个非常重要的概念,因此,本文主要针对接触角随热负荷的变化规律进行了可视化实验研究。 实验结果表明,接触角发生了明显的滞后现象;当加热功率较大时,接触角对加热功率的反应更为敏感蒸馏水－玻璃体系的接触角大于无水乙醇－玻璃体系的接触角。     

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By using Fluent software with the Eulerian multiphase model and Non-equilibrium boiling model, the subcooled flow boiling heat transfers was numerically simulated in the plain upward vertical tubes under the condition of one-side heating. The influences of the different mass flux, inlet temperatures and heat flux on the heat transfer coefficient, the void fraction and heat transfer deterioration were investigated.     

Dynamics of heat and mass transfer through a water-air interface based on measurements of thermal radio emission at a frequency of 60 GHz

We study the dynamics of heat and mass transfer through a water-air interface on the basis of laboratory radiometric measurements of the time dependence of thermal radio emission of water at a frequency of 60 GHz, which is related to air turbulization above its surface by a fan. We recover the dynamics for the temperature profile in water and in a viscous sublayer of air as well as for the heat flux through the water-air interface. The flux components related to evaporation and heat exchange and the rate of evaporation from a unit surface are determined. An equation for determining the thickness of the viscous sublayer in the air from the heat flux value is obtained;this thickness is about 2 mm under the experimental conditions. The process dependence on the water turbulence is established and methods for determining the thermal film thickness are proposed. In the absence of turbulence in unstable stratified water we observed the development of a periodic convective process from the time the critical value of the Rayleigh number was reached. The heat exchange dependence on the presence of petroleum film on the water surface is studied. It is found that for a film thickness of 5 μm the heat exchange rate decreases by a factor of 3 because of the petroleum presence. Radiophysical Research Institute, Nizhny Novgorod, Russia. Translated from Izvestiya Vysshikh Uchebnykh Zavedenii, Radiofizika, Vol. 40, No. 3, pp. 351–369, March, 1997.