Готові списки джерел за темами / Boiling of a liquid

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Автор: Grafiati
Опубліковано: 30 травня 2022
Оновлено: 31 травня 2022

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Статті в журналах з теми "Boiling of a liquid"

1

Lee, T. Y. Tom, Mali Mahalingam, and Peter J. C. Normington. "Subcooled Pool Boiling Critical Heat Flux in Dielectric Liquid Mixtures." Journal of Electronic Packaging 115, no. 1 (March 1, 1993): 134–37. http://dx.doi.org/10.1115/1.2909294.

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The beneficial effect of using dielectric liquid mixture in reducing temperature overshoot in pool boiling has been studied by the authors (Normington et al., 1992). The current experimental work addresses the influence of mixtures of dielectric liquids on the critical heat flux (CHF) in pool boiling. Two families of dielectric liquids were evaluated: perfluorocarbon liquids and perfluoropolyether liquids. Each set of the family consisted of two liquids with boiling points ranging from 80°C−110°C. Both 100 percent of each liquid and mixtures of two liquids were tested. Video filming was used along with electronic data collection. The perfluoropolyether liquids showed an increase in CHF as more high boiling liquid was added to the mixture, while the perfluorocarbon liquids had a constant CHF for all mixtures.
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2

Michiyoshi, I. "Boiling Heat Transfer in Liquid Metals." Applied Mechanics Reviews 41, no. 3 (March 1, 1988): 129–49. http://dx.doi.org/10.1115/1.3151887.

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This article presents the state-of-the-art review of boiling heat transfer in various liquid metals paying attention to research papers published in the last 15 years. Particular emphasis is laid on the incipient boiling superheat, diagnosis of natural and forced convection boiling, nucleate pool boiling heat transfer in mercury, sodium, potassium, NaK, lithium, and so on at sub- and near atmospheric pressure, effect of liquid level on liquid metal boiling, subcooling effect due to hydrostatic head on liquid metal boiling, effect of magnetic field on liquid metal boiling, pool boiling crisis under various conditions and intermittent boiling of liquid metal, two-phase flow heat transfer, and natural and forced convection film boiling in saturated and subcooled liquid metals. In conclusion, there still remain some ambiguous and unsolved problems which are pointed out in this article. Further studies are of course required to clarify and solve them in future with both theoretical and experimental approaches.
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3

Chen, Tailian, and Suresh V. Garimella. "Effects of Dissolved Air on Subcooled Flow Boiling of a Dielectric Coolant in a Microchannel Heat Sink." Journal of Electronic Packaging 128, no. 4 (February 1, 2006): 398–404. http://dx.doi.org/10.1115/1.2351905.

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The effects of dissolved air in the dielectric liquid FC-77 on flow boiling in a microchannel heat sink containing ten parallel channels, each 500μm wide and 2.5mm deep, were experimentally investigated. Experiments were conducted before and after degassing, at three flow rates in the range of 30-50ml∕min. The dissolved air resulted in a significant reduction in wall temperature at which bubbles were first observed in the microchannels. Analysis of the results suggests that the bubbles observed initially in the undegassed liquid were most likely air bubbles. Once the boiling process is initiated, the wall temperature continues to increase for the undegassed liquid, whereas it remains relatively unchanged in the case of the degassed liquid. Prior to the inception of boiling in the degassed liquid, the heat transfer coefficients with the undegassed liquid were 300-500% higher than for degassed liquid, depending on the flow rate. The heat transfer coefficients for both cases reach similar values at high heat fluxes (>120kW∕m2) once the boiling process with the degassed liquid was well established. The boiling process induced a significant increase in pressure drop relative to single-phase flow; the pressure drop for undegassed liquid was measured to be higher than for degassed liquid once the boiling process became well established in both cases. Flow instabilities were induced by the boiling process, and the magnitude of the instability was quantified using the standard deviation of the measured pressure drop at a given heat flux. It was found that the magnitude of flow instability increased with increasing heat flux in both the undegassed and degassed liquids, with greater flow instability noted in the undegassed liquid.
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4

Vasil’ev, N. V., Yu A. Zeigarnik, K. A. Khodakov, S. N. Vavilov, and A. S. Nikishin. "Studying of the characteristics of a single bubble under subcooled liquid boiling." Journal of Physics: Conference Series 2088, no. 1 (November 1, 2021): 012048. http://dx.doi.org/10.1088/1742-6596/2088/1/012048.

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Abstract An experimental study of the characteristics of single (solitary) bubbles obtained by means of focused laser heating of the surface during the boiling of two subcooled liquids with significantly different properties: water and refrigerant R113 has been carried out. To obtain the most complete detailed information, the technique of synchronized high-speed video filming of the process in two mutually perpendicular planes with a frame rate of up to 150 kHz was used. It is shown that during the boiling of a subcooled liquid, the main mechanism of heat removal from the bubble dome into the surrounding liquid is an unsteady heat conductance. Differences in the behavior of solitary vapor bubbles in the case of boiling of two liquids (water and refrigerant R113) are shown.
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5

Wang, Qing Yu, Song Qing Lin, Liu Shan Yang, Zhi Zhen Huang, Man Man Zhou, and Yan Dong Ma. "Influence of Liquid Mass on Purificating Sugar from Candied Liquid of Preserved Fruits with Evaporation Method." Advanced Materials Research 356-360 (October 2011): 1105–8. http://dx.doi.org/10.4028/www.scientific.net/amr.356-360.1105.

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In order to observe the influence of liquid mass with evaporating purification from candied liquid of preserved fruits in the same boiling time, volume were obtained 35 g, 40 g, 45 g, 50 g, 55 g of candied liquid to evaporate. Boiling the solution for each time for 25 mins, the quality of each of four groups of parallel experiments was done to measure the candied liquid evaporation after sugar, the effects of different quality candied liquid evaporation effect. The results showed that in the same boiling time, the increase in quality with liquid, sugar becomes larger and larger; Candied liquid boiling temperature is about 99 °C, liquid in the different quality of candied sugar by evaporation and purification process need different times to boiling; In these experiments, candied sugar solution used was 60.8% of the percentage content.
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6

Fukusako, S., T. Komoriya, and N. Seki. "An Experimental Study of Transition and Film Boiling Heat Transfer in Liquid-Saturated Porous Bed." Journal of Heat Transfer 108, no. 1 (February 1, 1986): 117–24. http://dx.doi.org/10.1115/1.3246875.

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Experimental investigations of transition and film boiling in a liquid-saturated porous bed are reported. The porous bed contained in a vertical circular cylinder is made up of packed spherical beads whose diameters range from 1.0 to 16.5 mm, while the depth of the bed overlying the heating surface varies from 10 to 300 mm. Water and fluorocarbon refrigerants R-11 and R-113 are adopted as testing liquids. Special attention is focused on the effect of the diameter of spherical beads on boiling heat transfer in the transition boiling region. It is found that for the small bead diameters the steady boiling heat transfer rises monotonically with temperature from nucleate boiling through the film boiling region, without going through a local maximum.
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7

Dragunov, Y., M. Bykov, Y. Bezrukov, S. Alekseenko, N. Pribaturin, S. Lezhnin, and A. Sorokin. "ICONE15-10610 INVESTIGATION OF BOILING LIQUID FLOW THROUGH PIPELINE BREAK." Proceedings of the International Conference on Nuclear Engineering (ICONE) 2007.15 (2007): _ICONE1510. http://dx.doi.org/10.1299/jsmeicone.2007.15._icone1510_333.

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8

Li, Hong, Liu Shan Yang, Yan Dong Ma, Zhi Zhen Huang, Man Man Zhou, and Song Qing Lin. "Influence of Boiling Time on Purifying Sugar from Preserved Fruits Candied Liquid with Evaporation Method." Advanced Materials Research 356-360 (October 2011): 1097–100. http://dx.doi.org/10.4028/www.scientific.net/amr.356-360.1097.

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In order to observe the influences of liquid boiling time on purifying sugar from candied liquid with evaporation method, 50 g of candied liquid was weighed for evaporating experiments and control of the boiling time is 10 min, 20 min, 25 min, 30 min. In these experiments, 6 parallel experiments were done at each boiling time for observing the change of the candied liquid in different boiling time and determining the sweetness of candied liquid. The results show that: with the increase of boiling time, sugar content continue to decrease; Selected time for the purity of the purified sugar have a great impact.
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9

Moraru, V. N. "THE MECHANISM OF RAISING AND QUANTIFICATION OF SPECIFIC HEAT FLUX AT BOILING OF NANOFLUIDS IN FREE CONVECTION CONDITIONS." Energy Technologies & Resource Saving, no. 3 (March 20, 2017): 25–34. http://dx.doi.org/10.33070/etars.3.2017.03.

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The results of our work and a number of foreign studies indicate that the sharp increase in the heat transfer parameters (specific heat flux q and heat transfer coefficient _) at the boiling of nanofluids as compared to the base liquid (water) is due not only and not so much to the increase of the thermal conductivity of the nanofluids, but an intensification of the boiling process caused by a change in the state of the heating surface, its topological and chemical properties (porosity, roughness, wettability). The latter leads to a change in the internal characteristics of the boiling process and the average temperature of the superheated liquid layer. This circumstance makes it possible, on the basis of physical models of the liquids boiling and taking into account the parameters of the surface state (temperature, pressure) and properties of the coolant (the density and heat capacity of the liquid, the specific heat of vaporization and the heat capacity of the vapor), and also the internal characteristics of the boiling of liquids, to calculate the value of specific heat flux q. In this paper, the difference in the mechanisms of heat transfer during the boiling of single-phase (water) and two-phase nanofluids has been studied and a quantitative estimate of the q values for the boiling of the nanofluid is carried out based on the internal characteristics of the boiling process. The satisfactory agreement of the calculated values with the experimental data is a confirmation that the key factor in the growth of the heat transfer intensity at the boiling of nanofluids is indeed a change in the nature and microrelief of the heating surface. Bibl. 20, Fig. 9, Tab. 2.
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10

Zou, Jintao, Hongguang Zhang, Zhenjiang Guo, Yawei Liu, Jiachen Wei, Yan Huang, and Xianren Zhang. "Surface Nanobubbles Nucleate Liquid Boiling." Langmuir 34, no. 46 (November 2018): 14096–101. http://dx.doi.org/10.1021/acs.langmuir.8b03290.

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Дисертації з теми "Boiling of a liquid"

1

Robinson, Anthony James Judd R. L. "Bubble growth dynamics in boiling /." *McMaster only, 2003.

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2

Reinke, Peter. "Surface boiling of superheated liquid /." Zürich, 1996. http://e-collection.ethbib.ethz.ch/show?type=diss&nr=11598.

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3

Giannini, Leonardo. "Boiling Liquid Expanding Vapor Explosion of liquid hydrogen." Master's thesis, Alma Mater Studiorum - Università di Bologna, 2022. http://amslaurea.unibo.it/25472/.

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This thesis focuses on the modelling of liquid hydrogen Boiling Liquid Expanding Vapor Explosions (BLEVEs). This terminology identifies a catastrophic release of this unconventional fuel following the loss of its containment. The present work aims to enhance the knowledge on the consequences of such explosions, using the data collected from crucial experiments to validate the simulations. The consequence analysis of the "SH2IFT Project" and the ”Bursting Tank Scenario” experimental BLEVEs is carried out simulating the explosions to verify the reliability of the implemented physical models. To complete the modeling of the catastrophic rupture of liquid hydrogen (LH2) tanks, the combustion process is taken into account to describe the aftermath of the simulated accidents in terms of overpressure and impulse. Furthermore, it is also discussed the possible involvement of the endothermic reaction of the hydrogen para-isomer converting into its ortho-isomer form. In this way, a further validation and confrontation between the models currently used for conventional liquid fuels like propane and liquefied petroleum gas (LPG) is possible, adopting and adapting them to the specific case of a liquid hydrogen catastrophic release. So, it is possible to consider this thesis as divided in three major steps: the first one is the analysis of the physical explosions with the proposed models, the second one is the adaptation of such models to take hydrogen combustion into consideration and the third and last one is an analysis of the para-ortho reaction which may follow the explosion. At the end, a confrontation between the experimental data and the proposed calculations is carried out, underlining the aspects which still require further studies, experiments and documentation.
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4

Barbone, Riccardo. "Explosive boiling of a depressurized volatile liquid." Thesis, McGill University, 1994. http://digitool.Library.McGill.CA:80/R/?func=dbin-jump-full&object_id=23444.

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The explosive boiling that occurs when a volatile liquid is suddenly vented to the atmosphere has been investigated experimentally. Refrigerant 22 is used as the test liquid and is depressurized from an initial state of equilibrium using a bursting foil diaphragm. The competition between the rates of venting and vapor generation can lead to substantial repressurization within the vessel. The influence of vent area, quantity of liquid, initial pressure and pre-nucleation on the explosive boiling characteristics has been studied in a 260 ml Teflon-coated vessel as well as in a 75 ml glass tube. The amount of repressurization is found to be proportional to the pressure drop which determines the degree of superheat attained by the liquid. The time for repressurization is typically an order of magnitude larger than the time for the pressure drop. The repressurization in both vessels reaches a maximum value at an initial saturation vapor pressure of $ approx$2 MPa. The dependence of the repressurization on initial pressure observed experimentally is found to be consistent with the predictions of a semi-empirical correlation based on homogeneous nucleation theory. High-speed photography shows that the mode of boiling is dependent on the initial vapor pressure and the surface condition of the vessel walls. Heterogeneous boiling from the walls dominates in the Teflon-coated steel vessel. For initial vapor pressures less than $ approx$1 MPa, an evaporation wave propagates at $ approx$0.15 m/s from the free surface throughout the length of the glass tube. For higher initial vapor pressures the boiling mode in the glass tube becomes predominantly heterogeneous. Pre-nucleation with CO$ sb2$ within the refrigerant increases the boiling response by promoting heterogeneous boiling.
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5

Ahmad, Hussain Hamed. "Boiling of immiscible systems over tube bundles." Thesis, Heriot-Watt University, 1989. http://hdl.handle.net/10399/966.

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6

Talari, Kiran. "LIQUID CRYSTAL THERMOGRAPHY STUDIES IN WATER POOL BOILING AT SUBATMOSPHERIC PRESSURES." Master's thesis, University of Central Florida, 2007. http://digital.library.ucf.edu/cdm/ref/collection/ETD/id/3388.

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A pool boiling experimental facility has been designed and built to investigate nucleate pool boiling in water under sub atmospheric pressure. Liquid crystal thermography, a non intrusive technique, is used for the determination of surface temperature distributions. This technique uses encapsulated liquid crystals that reflect definite colors at specific temperatures and viewing angle. Design of the test section is important in this experimental study. Since a new TLC is required for every new set of test conditions, a permanently sealed test section is not an option. The real challenge is to design a leak proof test section which is flexible so that it can be taken apart easily. A plexiglass test section, including a top chamber with an internal volume of 60.9 x 60.9 x 66.4 mm and a bottom plate of 5.5mm thickness is designed and assembled together using quick grips. In the test section, water is boiled using 85.0mm x 16.0mm and 0.050mm thick Fecralloy® as the heating element. The TLC sheet is attached to the bottom plate and the heating element is placed on top of TLC so that the temperature distribution of the heating element during boiling can be interpreted from TLC. A camera system fast enough to capture the thermal response of the TLC and an arrangement to capture both hue of the TLC and growth of the bubble on the same frame has been designed and successfully used. This system allowed recording of position, size and shape of the bubble with synchronized surface temperature. In order to get hue vs. temperature relation, in-situ calibration of the TLC is performed for each test condition with the present experimental setup and lighting conditions. It is found that the calibration curve of the TLC at atmospheric pressure is different from the calibration curve of the same TLC at subatmospheric pressures. The maximum temperature difference between the two curves for the same hue is found to be only 0.6°C. The experiment is run at four different test conditions of subatmospheric pressure and low heat flux. It is run at system pressures of 6.2kPa (0.89Psi) and 8.0kPa (1.16Psi) with a constant heat flux of 1.88kW/m2 and 2.70kW/m2, and a constant heat flux of 2.70kW/m2, 3.662kW/m2 and 4.50 kW/m2 respectively. Analysis of nucleating surface temperatures using thermochromic liquid crystal technique is performed for these test conditions and the bubble dynamics is studied. The temperature distribution is quite varied in each case and the temperature is at its maximum value at the center of the bubble and it decreases radially from the center. The dry spot observed during the experiments indicates that the process of evaporation of the microlayer is dominant at subatmospheric pressures. It is observed that at very low pressure and heat flux the bubble growth is accompanied by the neck formation. Boiling parameters such as bubble frequency, bubble size and contact are also analyzed and a summary of these results for four different test conditions is presented and the relevant differences between the cases are discussed and the effect of increase in pressure and heat flux is noted.
M.S.
Department of Mechanical, Materials and Aerospace Engineering;
Engineering and Computer Science
Mechanical Engineering
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7

Aligoodarz, M. R. "Flow boiling heat transfer in a single narrow channel." Thesis, University of Oxford, 1998. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.298767.

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8

Ament, David Lloyd. "Boiling heat transfer in thin liquid films with a wire mesh screen on the liquid surface." Thesis, Georgia Institute of Technology, 1994. http://hdl.handle.net/1853/19483.

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9

Gong, Shengjie. "An Experimental Study on Micro-Hydrodynamics of Evaporating/Boiling Liquid Film." Doctoral thesis, KTH, Kärnkraftsäkerhet, 2011. http://urn.kb.se/resolve?urn=urn:nbn:se:kth:diva-50216.

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Study of liquid film dynamics is of significant importance to the understanding and control of various industrial processes that involve spray cooling (condensation), heating (boiling), coating, cleaning and lubrication. For instance, the critical heat flux (CHF) of boiling heat transfer is one of the key parameters ensuring the efficiency and safety of nuclear power plants under both operational and accident conditions, which occurs as the liquid layers (microlayer and macrolayer) near the heater wall lose their integrity. However, an experimental quantification of thin liquid film dynamics is not straightforward, since the measurement at micro-scale is a challenge, and further complicated by the chaotic nature of boiling process. The object of present study is to develop experimental methods for the diagnosis of liquid film dynamics, and to obtain data for the film instability under various conditions. A dedicated test facility was designed and constructed where micro conductive probes and confocal optical sensors were used to measure the thickness and dynamic characteristics of a thin liquid film on various heater surfaces, while a high speed camera was used to get visual observation. Extensive tests were performed to calibrate and verify the two thickness measuring systems. The micro conductive measuring system was proven to have a high reliability and repeatability with maximum system error less than 5µm, while the optical measuring system is capable of recording the film dynamics with spatial resolution of less than 1 mm. The simultaneous measurement on the same liquid film shows that the two techniques are in a good agreement with respect to accuracy, but the optical sensors have a much higher acquisition rate up to 30 kHz, which are more suitable for rapid process. The confocal optical sensors were therefore employed to measure the dynamic thickness of liquid films (ethanol, hexane and water) evaporating on various horizontal heater surfaces (aluminum, copper, silicon, stainless steel and titanium) to investigate the influences of heat flux, the surface and liquid properties on the film instability and the critical thickness. The critical thickness of water film evaporating on various surfaces was measured in the range of 60-150 mm, increasing with the increased contact angle or increased heat flux (evaporating rate) and also with the decreased thermal conductivity of the heater material. The data suggest the conjugate heat transfer nature of the evaporating liquid film dynamics at higher heat fluxes of interest to boiling and burnout. In the case of hexane on the aged titanium surface with contact angle of ~3o, the liquid film is found resilient to rupture, with film oscillations at relatively large amplitude ensuing as the averaged film thickness decreases below 15 µm. To interpret our experimental findings on liquid film evolution and its critical thickness at rupture, a theoretical analysis is also performed to analyze the dynamics of liquid films evaporating on heater surfaces. While the influences of liquid properties, heat flux, and thermal conductivity of heater surface are captured by the simulation of the lubrication theory, influence of the wettability is considered via a minimum free energy criterion. The thinning processes of the liquid films are generally captured by the simulation of the lubrication theory. For the case with ideally uniform heat flux over the heater surface, the instability of the liquid film occurs at the thickness level of tens micro meters, while for the case of non-uniform heating, the critical thicknesses for the film rupture are closer to  the experimental data but still underestimated by the lubrication theory simulation. By introducing the minimum free energy criterion to considering the influence of surface wettability, the obtained critical thicknesses have a good agreement with the experimental ones for both titanium and copper surfaces, with a maximum deviation less than ±10%. The simulations also explain why the critical thickness on a copper surface is thinner than that on a titanium surface. It is because the good thermal conductivity of copper surface leads to uniform temperature distribution on the heat surface, which is responsible for the resilience of the liquid film to rupture. A silicon wafer with an artificial cavity fabricated by Micro Electronic Mechanical System (MEMS) technology was used as a heater to investigate the dynamics of a single bubble in both a thick and thin liquid layer under low heat flux (<60 kW/m2). The maximum departure diameter of an isolated bubble in a thick liquid film was measured to be 3.2 mm which is well predicted by the Fritz equation. However, in a thin liquid layer with its thickness less than the bubble departure diameter, the bubble was stuck on the heater surface with a dry spot beneath. A threshold thickness of the liquid film which enables the dry spot rewettable was obtained, and its value linearly increases with increasing heat flux. In addition, another test section was designed to achieve a constant liquid film flow on a titanium nano-heater surface which helps to successfully carry boiling in the liquid film from low heat flux until CHF. Again, the confocal optical sensor was employed to measure the dynamics of the liquid film on the heater surface under varied heat flux conditions.  A statistical analysis of the measured thickness signals that emerge in a certain period indicates three distinct liquid film thickness ranges: 0~50 µm as microlayer, 50~500 µm as macrolayer, 500~2500 µm as bulk layer. With increasing heat flux, the bulk layer disappears, and then the macrolayer gradually decreases to ~105 µm, beyond which instability of the liquid film may lose its integrity and CHF occurs. In addition, the high-speed camera was applied to directly visualize and record the bubbles dynamics and liquid film evolution. Dry spots were observed under some bubbles occasionally from 313 kW/m2 until CHF with the maximum occupation fraction within 5%.  A dry spot was rewetted either by liquid receding after the rupture of a bubble or by the liquid spreading from bubbles’ growth in the vicinity. This implies that the bubbles’ behavior (growth and rupture) and their interactions in particular are of paramount importance to the integrity of liquid film under nucleate boiling regime.
QC 20111205
VR-2005-5729, MSWI
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10

Glavin, Nicholas R. "Photonically Enhanced and Controlled Pool Boiling Heat Transfer." University of Dayton / OhioLINK, 2012. http://rave.ohiolink.edu/etdc/view?acc_num=dayton1343401685.

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Книги з теми "Boiling of a liquid"

1

Reinke, Peter. Surface boiling of superheated liquid. Villigen, Switzerland: Paul Scherrer Institute, Labor für Thermohydraulik, 1997.

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2

Boiling, condensation, and gas-liquid flow. Oxford [Oxfordshire]: Clarendon Press, 1987.

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3

Explosive boiling of superheated cryogenic liquids. Weinheim, DE: Wiley-VCH, 2007.

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4

Baĭdakov, V. G. Explosive boiling of superheated cryogenic liquids. Weinheim: Wiley-VCH, 2007.

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5

Theofanous, T. G. Performance of the liquid reactivity control system in BWRs. Washington, DC: Division of Regulatory Applications, Office of Nuclear Regulatory Research, U.S. Nuclear Regulatory Commission, 1989.

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6

Ghiaasiaan, Mostafa. Gas-liquid two-phase flow: Boiling and condensation in conventional, mini and micro systems. New York: Cambridge University Press, 2007.

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7

Sutton, Remar. Boiling Rock. Latham, N.Y: British American Pub., 1991.

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8

ill, Pollak Barbara, ed. Boiling point. New York: Grosset & Dunlap, 2002.

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9

Boiling point. New York: Jove Books, 2011.

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10

Toler, George S. Chechnya still boiling. New York: Nova Science Publishers, 2010.

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Частини книг з теми "Boiling of a liquid"

1

Kolev, Nikolay Ivanov. "Boiling of subcooled liquid." In Multiphase Flow Dynamics 3, 195–205. Berlin, Heidelberg: Springer Berlin Heidelberg, 2011. http://dx.doi.org/10.1007/978-3-642-21372-4_8.

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2

Skripov, V. P., and O. A. Isaev. "Explosive Boiling: Some Experimental Situations." In Adiabatic Waves in Liquid-Vapor Systems, 181–95. Berlin, Heidelberg: Springer Berlin Heidelberg, 1990. http://dx.doi.org/10.1007/978-3-642-83587-2_16.

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3

Boissin, J. C., J. J. Thibault, J. Roussel, and E. Faddi. "Boiling Heat Transfer and Peak Nucleate Boiling Flux in Liquid Helium." In Advances in Cryogenic Engineering, 607–16. Boston, MA: Springer US, 1995. http://dx.doi.org/10.1007/978-1-4757-0516-4_63.

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Zhang, Suojiang, Qing Zhou, Xingmei Lu, Yuting Song, and Xinxin Wang. "Boiling point of diethanolammonium chloride mixtures." In Physicochemical Properties of Ionic Liquid Mixtures, 1217–19. Dordrecht: Springer Netherlands, 2016. http://dx.doi.org/10.1007/978-94-017-7573-1_155.

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Zhang, Suojiang, Qing Zhou, Xingmei Lu, Yuting Song, and Xinxin Wang. "Boiling point of diethanolammonium acetate mixtures." In Physicochemical Properties of Ionic Liquid Mixtures, 1220–21. Dordrecht: Springer Netherlands, 2016. http://dx.doi.org/10.1007/978-94-017-7573-1_156.

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Zhang, Suojiang, Qing Zhou, Xingmei Lu, Yuting Song, and Xinxin Wang. "Boiling point of triethanolammonium acetate mixtures." In Physicochemical Properties of Ionic Liquid Mixtures, 1222–24. Dordrecht: Springer Netherlands, 2016. http://dx.doi.org/10.1007/978-94-017-7573-1_157.

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Barbone, R., D. L. Frost, A. Makris, and J. Nerenberg. "Explosive Boiling of a Depressurized Volatile Liquid." In IUTAM Symposium on Waves in Liquid/Gas and Liquid/Vapour Two-Phase Systems, 315–24. Dordrecht: Springer Netherlands, 1995. http://dx.doi.org/10.1007/978-94-011-0057-1_26.

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Gouin, H., and H. H. Fliche. "Film Boiling Phenomena in Liquid-Vapour Interfaces." In Adiabatic Waves in Liquid-Vapor Systems, 305–14. Berlin, Heidelberg: Springer Berlin Heidelberg, 1990. http://dx.doi.org/10.1007/978-3-642-83587-2_27.

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Zhang, Suojiang, Qing Zhou, Xingmei Lu, Yuting Song, and Xinxin Wang. "Boiling point of 2-hydroxyethylammonium acetate mixtures." In Physicochemical Properties of Ionic Liquid Mixtures, 1193–95. Dordrecht: Springer Netherlands, 2016. http://dx.doi.org/10.1007/978-94-017-7573-1_146.

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10

Ghajar, Afshin J. "Non-Boiling Two-Phase Heat Transfer." In Two-Phase Gas-Liquid Flow in Pipes with Different Orientations, 103–16. Cham: Springer International Publishing, 2020. http://dx.doi.org/10.1007/978-3-030-41626-3_7.

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Тези доповідей конференцій з теми "Boiling of a liquid"

1

Zhao, Zenghui, Corey Woodcock, Yoav Peles, and Michael K. Jensen. "Enhanced Liquid Jet Impingement Boiling." In ASME 2012 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2012. http://dx.doi.org/10.1115/imece2012-89265.

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Анотація:
In a previous study, it was shown that water jet impinging on structured-porous surface is a highly efficient way in dissipating high heat flux with small surface temperature increase. As an extension, this work studies jet impingement boiling on a plain surface and a porous surface using HFE-7000 as the working fluid. The effects of jet Reynolds number and jet inlet subcooling on heat transfer performance were explored with atmospheric experiments. The results show that, for plain surface, neither flow rate nor subcooling has significant effects on heat transfer performance when boiling is fully established; for porous surface, the effects of subcooling and jet Reynolds are more pronounced. In addition, CHF was reached during all experiments. Correlation was developed that can satisfactorily predict CHF for HFE-7000 jet impingement on plain copper surface.
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2

Dhillon, Navdeep Singh, Seyed Reza Mahmoudi, and Kripa Varanasi. "Video: Electrified amoebas in boiling liquid." In 67th Annual Meeting of the APS Division of Fluid Dynamics. American Physical Society, 2014. http://dx.doi.org/10.1103/aps.dfd.2014.gfm.v0095.

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3

Hirano, Hirokazu, Takamitsu Tajima, Takeru Hasegawa, Tsuyoshi Sekiguchi, and Minoru Uchino. "Boiling Liquid Battery Cooling for Electric Vehicle." In 2014 IEEE Transportation Electrification Conference and Expo, Asia-Pacific (ITEC Asia-Pacific). IEEE, 2014. http://dx.doi.org/10.1109/itec-ap.2014.6940931.

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4

Klausner, James F., Renwei Mei, and Wen Chin Chen. "Liquid crystal thermography in boiling heat transfer." In SPIE's 1995 International Symposium on Optical Science, Engineering, and Instrumentation, edited by Soyoung S. Cha and James D. Trolinger. SPIE, 1995. http://dx.doi.org/10.1117/12.221519.

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5

Kenning, D. B. R., M. Wienecke, and T. Kono. "BOILING HEAT TRANSFER BY LIQUID CRYSTAL THERMOGRAPHY." In Thermal Sciences 2000. Proceedings of the International Thermal Science Seminar Bled. Connecticut: Begellhouse, 2000. http://dx.doi.org/10.1615/ichmt.2000.thersieprocvol2thersieprocvol1.50.

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6

Haruyama, T. "Boiling heat transfer characteristics of liquid xenon." In ADVANCES IN CRYOGENIC ENGINEERING: Proceedings of the Cryogenic Engineering Conference - CEC. AIP, 2002. http://dx.doi.org/10.1063/1.1472183.

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7

Pinhasi, Gad, Abhaham Dayan, and Amos Ullmann. "Numerical Model for Boiling Liquid Vapor Explosion (BLEVE)." In 42nd AIAA Aerospace Sciences Meeting and Exhibit. Reston, Virigina: American Institute of Aeronautics and Astronautics, 2004. http://dx.doi.org/10.2514/6.2004-161.

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8

Hollingsworth, D. Keith. "Liquid Crystal Imaging of Flow Boiling in Minichannels." In ASME 2004 2nd International Conference on Microchannels and Minichannels. ASMEDC, 2004. http://dx.doi.org/10.1115/icmm2004-2320.

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Анотація:
Quantitative liquid crystal thermography was used to investigate boiling incipience and nucleate flow boiling in rectangular mini-channels with channel heights of 2 mm to 500 μm. Distributions of surface temperature along the heated surface were measured from the liquid crystal images, and streamwise profiles of heat transfer coefficient on the heated surface were calculated. The working fluid was the refrigerant R-11. Observations of the boiling incipience superheat excursion, the hysteresis phenomenon, and saturated flow boiling are presented. Comparisons to established two-phase heat transfer correlations are performed to investigate the existence of “thin channel” effects.
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9

Zhou, Peng, Yongqi Xu, and Xiuling Wang. "CFD Simulation of Pool Boiling for Liquid Nitrogen." In ASME 2017 Heat Transfer Summer Conference. American Society of Mechanical Engineers, 2017. http://dx.doi.org/10.1115/ht2017-4952.

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Computational Fluid Dynamics model is developed to simulate pool boiling for liquid nitrogen. Instead of using the user defined function (UDF), the evaporation-condensation model is adopted to take care of the energy term when phase change happens. Test cases with different excess temperature are simulated to study the important heat transfer features in different boiling regimes — free convection boiling, nucleate boiling, transition boiling and film boiling. The heat flux for each case is calculated. Simulation results are compared with the experimental and numerical data in the literature, good agreements are observed. By using the evaporation-condensation model, the pool boiling procedure is successfully simulated, and the complex physical process such as the pool vaporization can be clearly analyzed. At last, some comments and improvements are discussed to increase the accuracy of the simulation.
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10

Omar, Ahmed M. T., M. S. Hamed, and M. Shoukri. "Nucleate Boiling Heat Transfer Under Liquid Jet Impingement." In ASME/JSME 2007 Thermal Engineering Heat Transfer Summer Conference collocated with the ASME 2007 InterPACK Conference. ASMEDC, 2007. http://dx.doi.org/10.1115/ht2007-32020.

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Liquid jet impingement is a very effective way of cooling of simple and complicated geometry objects. The attainable cooling rate is radically enhanced when using liquids as coolant due to the possibility of having boiling to occur during the impingement process. Bubble activity on the surface and the resulted mixing with the fluid bulk produces an additional factor of enhancement which at some levels of surface temperature dominates other convective mechanism due to the coolant flow perpendicular or parallel to the surface. The efficient nucleate boiling heat transfer regime can be divided into: partial nucleate boiling and fully developed nucleate boiling. The heat transfer capacity of each and the range of surface temperature over which each of these two boiling regimes up to the critical heat flux (CHF) are experimentally investigated in this research for different coolant temperature and velocity. For this purpose, single planar jet is used to provide the cooling medium of a flat surface that is being heated steadily. The boiling surface temperature was thus controlled by a feed back computer program to allow for steady state operation. So, at each level of boiling surface temperature observation of boiling mode and heat transfer mechanisms was elongated and verified. The experiments were conducted using degassed water jet velocity range between 0.75 and 1.7 m/s and degree of sub-cooling range from 10 to 28 °C at atmospheric pressure. The variation of the heat flux with those factors at different surface superheat up to the CHF point is presented. A physical interpretation is introduced to explain the effects of the input parameters on the heat transfer changes in these regimes.
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Звіти організацій з теми "Boiling of a liquid"

1

PACE, M. E. LIQUID PROPANE GAS (LPG) STORAGE AREA BOILING LIQUID EXPANDING VAPOR EXPLOSION (BLEVE) ANALYSIS. Office of Scientific and Technical Information (OSTI), January 2004. http://dx.doi.org/10.2172/820866.

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2

Narumanchi, S. V. J., V. Hassani, and D. Bharathan. Modeling Single-Phase and Boiling Liquid Jet Impingement Cooling in Power Electronics. Office of Scientific and Technical Information (OSTI), December 2005. http://dx.doi.org/10.2172/861486.

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3

Theofanous, T., and E. Shabana. Performance of the liquid reactivity control system in BWRs (boiling water reactors). Office of Scientific and Technical Information (OSTI), September 1989. http://dx.doi.org/10.2172/5387472.

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4

Pruess, Karsten. Numerical simulation of CO2 leakage from a geologic disposal reservoir including transitions from super- to sub-critical conditions, and boiling of liquid of CO2. Office of Scientific and Technical Information (OSTI), March 2003. http://dx.doi.org/10.2172/813575.

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5

Duell, Anna. Analysis of E-cigarette Liquids and Aerosols by NMR Spectroscopy: Compositions, Boiling Points, and Degradation Profiles. Portland State University Library, January 2000. http://dx.doi.org/10.15760/etd.7224.

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6

Aritomi, Masanori, Takatoshi Takemoto, and Jing-Hsien Chiang. Geysering in boiling channels. Office of Scientific and Technical Information (OSTI), September 1995. http://dx.doi.org/10.2172/107753.

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7

Kim, Seung Jun. Assessment on DNB performance for high pressure subcooled boiling with modified CASL boiling model. Office of Scientific and Technical Information (OSTI), August 2019. http://dx.doi.org/10.2172/1558959.

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8

Mcculloch, Quinn. Microfluidic Liquid-Liquid Contactors. Office of Scientific and Technical Information (OSTI), July 2017. http://dx.doi.org/10.2172/1373499.

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9

Greenspan, Ehud, Phillip M. Gorman, Sandra Bogetic, Jeffrey E. Seifried, Guanheng Zhang, Christopher R. Varela, Massimiliano Fratoni, et al. Self-Sustaining Thorium Boiling Water Reactors. Office of Scientific and Technical Information (OSTI), March 2015. http://dx.doi.org/10.2172/1183773.

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10

Ott, L. J. (Boiling water reactor (BWR) CORA experiments). Office of Scientific and Technical Information (OSTI), October 1990. http://dx.doi.org/10.2172/6434331.

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