Relevant bibliographies by topics / Forced-convective boiling

Academic literature on the topic 'Forced-convective boiling'

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Published: 10 December 2022
Last updated: 28 January 2023

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Journal articles on the topic "Forced-convective boiling"

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Celata, Gian Piero, Maurizio Cumo, and Tommaso Setaro. "Forced convective boiling in binary mixtures." International Journal of Heat and Mass Transfer 36, no. 13 (September 1993): 3299–309. http://dx.doi.org/10.1016/0017-9310(93)90012-u.

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HIHARA, Eiji, Kazuhiro TANIDA, and Takamoto SAITO. "Forced Convective Boiling Experiments f Binary Mixtures." JSME international journal. Ser. 2, Fluids engineering, heat transfer, power, combustion, thermophysical properties 32, no. 1 (1989): 98–106. http://dx.doi.org/10.1299/jsmeb1988.32.1_98.

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Hwang, T. H., and S. C. Yao. "Forced convective boiling in horizontal tube bundles." International Journal of Heat and Mass Transfer 29, no. 5 (May 1986): 785–95. http://dx.doi.org/10.1016/0017-9310(86)90130-4.

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Bennett, D. L., B. L. Hertzler, and C. E. Kalb. "Down-flow shell-side forced convective boiling." AIChE Journal 32, no. 12 (December 1986): 1963–70. http://dx.doi.org/10.1002/aic.690321205.

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MONDE, Masanori, and Yohichi FURUKAWA. "Critical heat flux in saturated forced convective boiling with an impinging jet. (Coexistence of pool and forced convective boilings)." Transactions of the Japan Society of Mechanical Engineers Series B 53, no. 485 (1987): 199–203. http://dx.doi.org/10.1299/kikaib.53.199.

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WEI Ji-feng, 魏继锋, 高学燕 GAO Xue-yan, 张凯 ZHANG Kai, 周山 ZHOU Shan, 何均章 HE Jun-zhang, and 关有光 GUAN You-guang. "Forced Convective Boiling Model of Water by Laser." ACTA PHOTONICA SINICA 39, no. 8 (2010): 1438–42. http://dx.doi.org/10.3788/gzxb20103908.1438.

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BADUGE, Sumith, Fumito KAMINAGA, and Kunihito MATSUMURA. "1115 Forced Convective Boiling in a Capillary Tube." Proceedings of Conference of Kanto Branch 2002.8 (2002): 519–20. http://dx.doi.org/10.1299/jsmekanto.2002.8.519.

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ISHIGAKI, Hideyuki, and Yuichi FUNAWATASHI. "408 Forced Convective Boiling Heat Transfer in Microchannels." Proceedings of Conference of Hokuriku-Shinetsu Branch 2010.47 (2010): 137–38. http://dx.doi.org/10.1299/jsmehs.2010.47.137.

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Strayer, T. D., G. M. Burdick, R. W. Dacus, T. Gallaway, B. L. Magolan, and B. M. Waite. "Four field flow modeling of forced convective boiling." Nuclear Engineering and Design 367 (October 2020): 110740. http://dx.doi.org/10.1016/j.nucengdes.2020.110740.

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Celata, Gian Piero, Maurizio Cumo, and Tommaso Setaro. "Vertical forced convective boiling of refrigerant binary mixtures." Revue Générale de Thermique 36, no. 4 (April 1997): 253–63. http://dx.doi.org/10.1016/s0035-3159(97)80686-1.

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Dissertations / Theses on the topic "Forced-convective boiling"

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Sun, Guang. "Heat transfer in forced convective flow boiling." Thesis, Imperial College London, 1996. http://hdl.handle.net/10044/1/11255.

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Kandlbinder, Thomas. "Experimental investigation of forced convective boiling of hydrocarbons and hydrocarbon mixtures." Thesis, Imperial College London, 1998. http://hdl.handle.net/10044/1/7918.

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Ahmad, Masroor. "Critical heat flux and associated phenomena in forced convective boiling in nuclear systems." Thesis, Imperial College London, 2012. http://hdl.handle.net/10044/1/9181.

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In evaporation of a liquid flowing in a tube or nuclear fuel element, there exists a transition (known as "dryout", "burnout", "boiling crisis" or "critical heat flux", CHF) from a high heat transfer coefficient regime to one of greatly reduced heat transfer coefficient. The conditions leading to dryout or CHF and the behaviour of wall temperatures in the ("post dryout or post CHF") region beyond it are of immense importance in nuclear reactor safety. In a nuclear reactor, the clad temperature excursion in the post-dryout region may be unacceptably high and the prediction of the location of dryout and the magnitude of the temperature excursion into the post-dryout region is of great importance. Moreover, the dryout transition and its effects are important not only in nuclear plant but also in many other types of heat transfer equipment. The main focus of work described in this thesis was the improvement and validation of phenomenological models for the prediction of CHF and of heat transfer beyond CHF ("post CHF" or "post dryout" heat transfer). The main focus has been on the process of annular film dryout. In phenomenological modelling of this process the dryout location prediction is sensitive to the boundary value of entrained fraction at churn annular transition, especially at high flow rates. The model was extended to churn flow so that integration of entrainment, deposition and evaporation processes could be started from onset of churn flow. A new correlation for the prediction of entrainment rate in churn flow was presented. The application of the new methodology to experimental data leads to improved predictions of CHF. Another long-standing problem, i.e. effect of heat flux on droplet entrainment, is addressed by analysing the contradictory results of previous experiments by using the annular film dryout model. The capability of phenomenological models to cover the whole range of CHF scenarios, i.e. from subcooled or very low quality to very high quality CHF, was demonstrated by using a possible transition criterion from bubble crowding model (an improved version of the Weisman Pie model) to annular film dryout model. These improved phenomenological models captured trends of CHF data very well (including the Look Up Table data of Groeneveld et al. 2007) and produced improved results over a wide range of system parameters such as pressure, mass flux and critical quality. The implementation of the phenomenological models was pursued by modifying and developing an Imperial College computer code GRAMP. In addition to its application in modelling CHF, the GRAMP code was extended to the post dryout region and predictions for this region compared to a range of data and the results were found to be satisfactory.
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Kiameh, Bassam Philip. "Prediction of critical heat flux (CHF) for non-aqueous fluids in forced convective boiling." Thesis, University of Ottawa (Canada), 1986. http://hdl.handle.net/10393/21731.

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De, Vos Wouter Philip. "Experimental determination of the forced convective boiling heat transfer coefficients of R407C in fluted-tubes / Philip Wouter de Vos." Thesis, North-West University, 2006. http://hdl.handle.net/10394/1035.

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Due to the phase-out of all refrigerants with ozone depletion potential, a large void is left in the refrigeration market. This void was caused due to a lack of new, ozone friendly, pure refrigerants with similar thermodynamic properties to those of the banned refrigerants. As a result mixtures of refrigerants are used to create replacement refrigerants. These new mixtures have to be experimentally evaluated to derive correlations for the prediction of the heat transfer coefficients. One of these mixtures is R407C. With this new refrigerant and the need for smaller, more compact heat exchangers, a search was initiated for a correlation describing the heat transfer coefficients of R4O7C in fluted-tube compact heat exchangers. The need for such a correlation is to accurately design compact fluted-tube heat exchangers for use in heat pumps and refrigeration systems. Fluted-tube heat exchangers are in general, much smaller and more compact than standard smooth tube-in-tube heat exchangers. The purpose of this study was to experimentally determine the forced convective boiling heat transfer coefficients of R407C in fluted-tubes; furthermore, to test these experimental values against existing heat transfer correlations. The product of this study is experimental boiling data for R22 and R407C in fluted-tubes, together with a correlation to predict the boiling heat transfer coefficient of R4O7C in fluted-tubes. The test bench used, was a 15 kW heat pump with a split evaporator design. The split evaporator is made up of a bypass evaporator and a test evaporator, with the test evaporator consisting of three separate heat exchangers: the pre-evaporator, test section and the super-heater. Of the three heat exchangers only the test section was a fluted tube-in-tube heat exchanger with the other two smooth tube-in-tube heat exchangers. The test section was operated in a counter flow configuration with water flowing inside the fluted-tube and the refrigerant flowing in the annulus. The accuracy of the test bench was validated using R22 in a smooth tube-in-tube heat exchanger, resulting in a maximum deviation between the water and the refrigerant heat transfer of 2.5%. After the validation the smooth tube test section was replaced with the fluted-tube section and tested with R22 and R407C. The refrigerant mass flow rates ranged from 0.01 kg/s - 0.03 kg/s. Along with the mass flow rates the heat fluxes were varied from 0.89 kW/m2 - 20.34 kW/m2 and with evaporating pressures set at 4.0, 4.5, 5.0 and 5.5 bar respectively. The maximum deviation between the water heat transfer and the refrigerant heat transfer for all the tests was 2.77% with an overall average deviation of 0.83%. The experimental results for R22 and R407C were evaluated against seven correlations found in the literature consulted: Gungor and Winterton (1986:351), Gungor and Winterton (1 987: l48), Liu and Winterton (1 991 :2759), Pierre (ASHRAE Fundamentals, 1997:4.7), Chen (1963: I), Rousseau et al. (2003:232) and Kattan et al. (1 998c: 156). All the correlations were used as found in the literature, with the exception on the Rousseau et al. (2003:232) correlation. The enhancement factor used in this correlation was adapted to fit the experimental data better. Comparing results of all the correlations, it was found that Rousseau et al. (2003:232), with the adapted enhancement factor, gave the best results for R22 as well as R407C, with the respective average deviations of 12.67% and 3.83% and respective mean deviations of 35.16% and 22.01%. A new correlation was proposed combining the geometric properties of the Rousseau et al. (2003:232) correlation with the boiling heat transfer of the Gungor and Winterton (1 987: 148) correlation.
Thesis (M. Ing. (Mechanical Engineering))--North-West University, Potchefstroom Campus, 2006.
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Ahn, Hee Seok. "Heat transfer enhancement in single-phase forced convection with blockages and in two-phase pool boiling with nano-structured surfaces." Texas A&M University, 2003. http://hdl.handle.net/1969.1/5869.

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The first study researched turbulent forced convective heat (mass) transfer down- stream of blockages with round and elongated holes in a rectangular channel. The blockages and the channel had the same cross section, and a distance equal to twice the channel height separated consecutive blockages. Naphthalene sublimation experiments were conducted with four hole aspect ratios (hole-width-to-height ratios) and two hole-to-blockage area ratios (ratios of total hole cross-sectional area to blockage area). The effects of the hole aspect ratio, for each hole-to-blockage area ratio, on the local heat (mass) transfer distribution on the exposed primary channel wall between consecutive blockages were examined. Results showed that the blockages with holes enhanced the average heat (mass) transfer by up to 8.5 and 7.0 times that for fully developed turbulent flow through a smooth channel at the same mass flow rate, respectively, in the smaller and larger hole-to-blockage area ratio (or smaller and larger hole diameter) cases. The elongated holes caused a higher average heat (mass) transfer and a larger spanwise variation of the local heat (mass) transfer on the channel wall than did the round holes. The second study explored the heat transfer enhancement for pool boiling on nano-structured surfaces. Experiments were conducted with three horizontal silicon surfaces, two of which were coated with vertically aligned multi-walled carbon nanotubes (MWCNT) with heights of 9 and 25 ¹m, respectively, and diameters between 8 and 15 nm. The MWCNT arrays were synthesized on the two silicon wafers using chemical vapor deposition. Experimental results were obtained over the nucleate boiling and film boiling regimes under saturated and sub-cooled (5±C and 10±C) boiling conditions. PF-5060 was the test fluid. Results showed that the MWCNT array with a height of 25 ¹m enhanced the nucleate and film boiling heat fluxes on the silicon surface by up to 380% and 60%, respectively, under saturated boiling conditions, and by up to 300% and 80%, respectively, under 10±C sub-cooled boiling conditions, over corresponding heat fluxes on a smooth silicon surface. The MWCNT array with a height of 9 ¹m enhanced the nucleate boiling heat flux as much as the taller array, but did not significantly enhance the wall heat flux in the film boiling regime.
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HUANG, NAN-SEN, and 黃錦鎰. "Transient void fraction response in a forced convective boiling system." Thesis, 1987. http://ndltd.ncl.edu.tw/handle/26093171315802387879.

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Books on the topic "Forced-convective boiling"

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Thorncroft, Glen. Heat Transfer and Vapor Bubble Dynamics in Forced Convective Boiling. Creative Media Partners, LLC, 2019.

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Thorncroft, Glen. Heat Transfer and Vapor Bubble Dynamics in Forced Convective Boiling. Dissertation Discovery Company, 2019.

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Book chapters on the topic "Forced-convective boiling"

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Yu, Wenhua, David M. France, and Jules L. Routbort. "Forced Convective Boiling of Ethylene Glycol/Water Mixtures Inside a Small Tube." In Film and Nucleate Boiling Processes, 376–401. 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959: ASTM International, 2011. http://dx.doi.org/10.1520/stp49346t.

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Yu, Wenhua, David M. France, and Jules L. Routbort. "Forced Convective Boiling of Ethylene Glycol/Water Mixtures Inside a Small Tube." In Film and Nucleate Boiling Processes, 376–401. 100 Barr Harbor Drive, PO Box C700, West Conshohocken, PA 19428-2959: ASTM International, 2011. http://dx.doi.org/10.1520/stp153420120017.

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Thome, John R., and Andrea Cioncolini. "Forced Convective Boiling." In Encyclopedia of Two-Phase Heat Transfer and Flow I, 177–218. WORLD SCIENTIFIC, 2015. http://dx.doi.org/10.1142/9789814623216_0024.

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Hewitt, Geoffrey F. "Pheomenological Issues in Forced Convective Boiling." In Convective Flow Boiling, 3–14. CRC Press, 2019. http://dx.doi.org/10.1201/9780367812089-1.

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Steiner, Dieter. "Forced Convective Vaporization of Saturated Liquid Mixtures." In Convective Flow Boiling, 271–76. CRC Press, 2019. http://dx.doi.org/10.1201/9780367812089-37.

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Chen, Haiyan, and Yuzhou Chen. "Forced Convective Heat Transfer to Superheated Steam in Round Tube." In Convective Flow Boiling, 243–48. CRC Press, 2019. http://dx.doi.org/10.1201/9780367812089-33.

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Celata, Glan Plero, Maurizio Cumo, and Tommaso Setaro. "Heat Transfer in Vertical Forced Convective Boiling of Binary Mixtures." In Convective Flow Boiling, 251–57. CRC Press, 2019. http://dx.doi.org/10.1201/9780367812089-34.

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Hijikata, Kunio, Takao Nagasaki, and Masayuki Hinokuma. "Free and Forced Convective Boiling Heat Transfer from a Small Heating Element." In Convective Flow Boiling, 299–304. CRC Press, 2019. http://dx.doi.org/10.1201/9780367812089-41.

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Stängl, G., and F. Mayinger. "Void Fraction and Recondensation Rate in Subcooled Forced Convective Boiling with Freon R12." In Convective Flow Boiling, 99–104. CRC Press, 2019. http://dx.doi.org/10.1201/9780367812089-10.

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Koyama, Sh, J. Yu, S. Momoki, T. Fujii, and H. Honda. "Forced Convective Flow Boiling Heat Transfer of Pure Refrigerants Inside a Horizontal Microfin Tube." In Convective Flow Boiling, 137–42. CRC Press, 2019. http://dx.doi.org/10.1201/9780367812089-16.

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Conference papers on the topic "Forced-convective boiling"

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Zheng, Qiang, Puzhen Gao, and Jian Hu. "Bubble Growth During Subcooled Forced Convective Flow Boiling." In 2013 21st International Conference on Nuclear Engineering. American Society of Mechanical Engineers, 2013. http://dx.doi.org/10.1115/icone21-16200.

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The inception, growth and collapse of vapor bubbles were observed and measured by using visual method under subcooled flow nucleation. The test section was a single-side heated rectangular channel by the scale of 2×40×700mm and the working fluid was clean water. The working condition was set as: the inlet subcooling Δ Tin = 330 °C, the mass flux m = 694kg/(m2s), the heat flux q = 210kW/m2 and the absolute pressure p = 0.22MPa. A high speed camera was used to record the bubble behaviors at the speed of 5000fps (frame per second). The results showed that the bubble lifetime was from 0.4ms to 2.2ms and the fraction of bubble with short lifetime was bigger than that of long lifetime. The bubble’s average diameter showed a linear relationship with the lifetime and it was also found that the sliding bubble would enhance heat transfer.
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Situ, R., J. Y. Tu, Guan Heng Yeoh, Goon Cherl Park, T. Hibiki, and Mamoru Ishii. "BUBBLE DEPARTURE IN FORCED CONVECTIVE SUBCOOLED BOILING FLOW." In Annals of the Assembly for International Heat Transfer Conference 13. Begell House Inc., 2006. http://dx.doi.org/10.1615/ihtc13.p28.220.

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Chu, In-Cheol, and Chul-Hwa Song. "Bubble Lift-Off Diameter in Forced Convective Boiling Flow." In 2010 14th International Heat Transfer Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/ihtc14-23024.

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A series of experiments were carried out to investigate the bubble nucleation to lift-off phenomena for a subcooled boiling flow in a vertical annulus channel. A high speed digital video camera was used to capture the dynamics of the bubble nucleation to lift-off process. A total of 148 recordings were made, and the bubble lift-off diameter and the bubble nucleation frequency were evaluated for 118 recordings up to now. The basic features of the lift-off diameter and nucleation frequency were addressed based on the present observation. A database for the bubble lift-off diameter was built by gathering and summarizing the data of Prodanovic et al., Situ et al., and the present work. The prediction capability of Unal’s model, Situ et al.’s model, and Prodanovic et al.’s correlation was evaluated against the database. The best prediction results were obtained by modifying the wall superheat correlation in Unal’s model.
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Situ, R., T. Hibiki, Mamoru Ishii, M. Mori, J. Y. Tu, Guan Heng Yeoh, and Goon Cherl Park. "BUBBLE LIFT-OFF IN FORCED CONVECTIVE SUBCOOLED BOILING FLOW." In Annals of the Assembly for International Heat Transfer Conference 13. Begell House Inc., 2006. http://dx.doi.org/10.1615/ihtc13.p28.210.

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Araga, Koichi, Keisuke Okamoto, and Keiji Murata. "Forced Convective Boiling of Refrigerant HCFC123 in a Mini-Tube." In 2010 14th International Heat Transfer Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/ihtc14-22060.

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This paper presents an experimental investigation of the forced convective boiling of refrigerant HCFC123 in a mini-tube. The inner diameters of the test tubes, D, were 0.51 mm and 0.30 mm. First, two-phase frictional pressure drops were measured under adiabatic conditions and compared with the correlations for conventional tubes. The frictional pressure drop data were lower than the correlation for conventional tubes. However, the data were qualitatively in accord with those for conventional tubes and were correlated in the form φL2−1/Xtt. Next, heat transfer coefficients were measured under the conditions of constant heat flux and compared with those for conventional tubes and for pool boiling. The heat transfer characteristics for mini-tubes were different from those for conventional tubes and quite complicated. The heat transfer coefficients for D = 0.51 mm increased with heat flux but were almost independent of mass flux. Although the heat transfer coefficients were higher than those for a conventional tube with D = 10.3 mm and for pool boiling in the low quality region, they decreased gradually with increasing quality. The heat transfer coefficients for D = 0.30 mm were higher than those for D = 0.51 mm and were almost independent of both mass flux and heat flux.
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Faulkner, Daniel J., and Reza Shekarriz. "Forced Convective Boiling in Microchannels for kW/cm2 Electronics Cooling." In ASME 2003 Heat Transfer Summer Conference. ASMEDC, 2003. http://dx.doi.org/10.1115/ht2003-47160.

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This paper reports some of the results of our tests for the development of a high heat flux cooling system for thermal management of high power electronics. Our objective is to develop a practical design solution for achieving 1000 W/cm2 cooling. To achieve such high heat transfer rates, we have pursued and combined design advantages of a microchannel heat exchanger, high heat fluxes associated with forced convective nucleate boiling, and the use of a nanoparticles laden fluid for enhancement of heat transfer. A laboratory test module was designed, built, and tested to verify its performance. The experimental system employed sub-cooled as well as saturated forced convection boiling heat transfer in a high aspect ratio parallel microchannel heat sink. The working fluids tested were water and a selection of ceramic-based nanoparticle suspensions (nanofluids). The system was observed to readily dissipate heat fluxes in excess of 275 W/cm2 of substrate, while maintaining the substrate at or below 125°C. For optimized fin geometry, the current conditions would result in greater than 500 W/cm2. While the use of nanofluids was intended for boiling enhancement to push the envelop beyond 1000 W/cm2, we discerned limited improvement in the overall heat transfer rate. Future studies are planned for further exploitation of nanoparticles for enhancement of convective nucleate boiling.
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Kunugi, Tomoaki, Nao Saito, Yoshitsugu Fujita, and Akimi Serizawa. "Direct numerical simulation of pool and forced convective flow boiling phenomena." In International Heat Transfer Conference 12. Connecticut: Begellhouse, 2002. http://dx.doi.org/10.1615/ihtc12.2290.

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Hihara, Eiji, and Takamoto Saito. "FORCED CONVECTIVE BOILING HEAT TRANSFER OF BINARY MIXTURES IN A HORIZONTAL TUBE." In International Heat Transfer Conference 9. Connecticut: Begellhouse, 1990. http://dx.doi.org/10.1615/ihtc9.210.

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Hosaka, S., Masaru Hirata, and Nobuhide Kasagi. "FORCED CONVECTIVE SUBCOOLED BOILING HEAT TRANSFER AND CHF IN SMALL-DIAMETER TUBES." In International Heat Transfer Conference 9. Connecticut: Begellhouse, 1990. http://dx.doi.org/10.1615/ihtc9.220.

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Monde, Masanori, Koji Kitaguchi, T. Inoue, and Yuichi Mitsutake. "CRITICAL HEAT FLUX IN A FORCED CONVECTIVE SUBCOOLED BOILING WITH AN IMPINGING JET." In International Heat Transfer Conference 10. Connecticut: Begellhouse, 1994. http://dx.doi.org/10.1615/ihtc10.1380.

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Reports on the topic "Forced-convective boiling"

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Wong, Christopher F. A computer code for calculating subcooled boiling pressure drop in forced convective tube flows. Office of Scientific and Technical Information (OSTI), December 1988. http://dx.doi.org/10.2172/5910189.

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