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Journal articles on the topic 'Forced-convective boiling'

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Published: 10 December 2022

Last updated: 28 January 2023

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1

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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2

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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3

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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4

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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5

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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6

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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7

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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8

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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9

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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10

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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11

Murata, K., and K. Hashizume. "Forced Convective Boiling of Nonazeotropic Refrigerant Mixtures Inside Tubes." Journal of Heat Transfer 115, no. 3 (August 1, 1993): 680–89. http://dx.doi.org/10.1115/1.2910739.

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Forced convective boiling of nonazeotropic mixtures inside horizontal tubes was investigated experimentally. The heat transfer coefficient and pressure drop of pure refrigerant R123 and a mixture of R123 and R134a were measured in both a smooth tube and a spirally grooved tube. The heat transfer coefficient for the mixture was found to be lower than that for an equivalent pure refrigerant with the same phsycial properties, not only in the boiling-dominant region but also in the convection-dominant region. On the basis of this experiment, correlations were proposed for heat transfer coefficients in smooth and grooved tubes; the reduction in heat transfer coefficient for the mixture is attributed to the mixture effects on nucleate boiling and to the heat transfer resistance in the vapor phase. This heat transfer resistance is caused by the sensible heating of the vapor phase accompanying the rise in saturation temperature. These correlations are able to predict the heat transfer data within ± 20 percent

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12

Situ, Rong, Jiyuan Tu, Guan Heng Yeoh, Takashi Hibiki, Mamoru Ishii, and Michitsugu Mori. "ICONE15-10148 DIMENSIONLESS ANALYSIS OF BUBBLE DEPARTURE FREQUENCY IN FORCED CONVECTIVE SUBCOOLED BOILING FLOW." Proceedings of the International Conference on Nuclear Engineering (ICONE) 2007.15 (2007): _ICONE1510. http://dx.doi.org/10.1299/jsmeicone.2007.15._icone1510_61.

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13

Bergles, A. E. "Heat Transfer Enhancement—The Encouragement and Accommodation of High Heat Fluxes." Journal of Heat Transfer 119, no. 1 (February 1, 1997): 8–19. http://dx.doi.org/10.1115/1.2824105.

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This review considers the many techniques that have been developed to enhance convective heat transfer. After introducing the techniques, the applications to most of the modes of heat transfer (single-phase forced convection, including compound techniques, pool boiling, convective boiling/evaporation, vapor-space condensation, and convective condensation) are described. Comments are offered regarding commercial introduction of this technology and the generations of heat transfer technology; advanced enhancement represents third-generation heat transfer technology.

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14

NAGAI, Niro, Kenta SUGIYAMA, Masanori TAKEUCHI, Shinji YOSHIKAWA, and Fujio YAMAMOTO. "Forced Convective Boiling of Water inside Helically Coiled Tube." Progress in Multiphase Flow Research 1 (2006): 111–18. http://dx.doi.org/10.3811/pmfr.1.111.

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15

Barbosa, J. R., T. Kandlbinder, and G. F. Hewitt. "Forced convective boiling of ternary mixtures at high qualities." International Journal of Heat and Mass Transfer 45, no. 13 (June 2002): 2655–65. http://dx.doi.org/10.1016/s0017-9310(01)00361-1.

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16

Situ, R., M. Ishii, T. Hibiki, J. Y. Tu, G. H. Yeoh, and M. Mori. "Bubble departure frequency in forced convective subcooled boiling flow." International Journal of Heat and Mass Transfer 51, no. 25-26 (December 2008): 6268–82. http://dx.doi.org/10.1016/j.ijheatmasstransfer.2008.04.028.

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17

Fujita, Yasunobu, and Hironobu Deguchi. "Forced convective boiling of subcooled water at high velocity." Heat Transfer - Japanese Research 27, no. 5 (1998): 376–89. http://dx.doi.org/10.1002/(sici)1520-6556(1998)27:5<376::aid-htj5>3.0.co;2-s.

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18

Davidy, Alon. "CFD Simulation of Forced Recirculating Fired Heated Reboilers." Processes 8, no. 2 (January 22, 2020): 145. http://dx.doi.org/10.3390/pr8020145.

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An advanced algorithm has been developed in order to analyze the performance of re-boiling process of crude oil flowing inside reboilers tubes. The proposed model is composed from Heptane fire heater and a tube array. The heat flux produced from burner is transferred to the crude oil flowing inside the tube. The computational model is composed of two phases—Simulation of fire by using Fire Dynamics Simulator software (FDS) version 5.0 and then a nucleate boiling computation of the crude oil. FDS code is formulated based on CFD (Computational Fluid Dynamics) of fire heater. The thermo-physical properties (such as: thermal conductivity, heat capacity, surface tension, viscosity) of the crude oil were estimated by using empirical correlations. The thermal heat transfer to evaporating two-phase crude oil mixture occur by bubble generation at the wall (nucleate boiling) has been calculated by using Chen correlation. It has been assumed that the overall convective heat transfer coefficient is composed from the nucleate boiling convective coefficient and the forced turbulent convective coefficient. The former is calculated by Forster Zuber empirical equation. The latter is computed from the Dittus-Boelter relationship. In order to validate the nucleate boiling heat transfer coefficient, a comparison has been performed to nucleate boiling convective coefficient obtained by Mostinski equation. The relative error between the nucleate boiling convective heat-transfer coefficients is 10.5%. The FDS numerical solution has been carried out by using Large Eddy Simulation (LES) method. This work has been further extended to include also the structural integrity aspects of the reboiler metal pipe by using COMSOL Multiphysics software. It was found out, that the calculated stress is less than the ultimate tensile strength of the AISI 310 Steel alloy.

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19

Kim, Seol Ha, In Cheol Chu, Moon Hee Choi, and Dong Jin Euh. "Mechanism study of departure of nucleate boiling on forced convective channel flow boiling." International Journal of Heat and Mass Transfer 126 (November 2018): 1049–58. http://dx.doi.org/10.1016/j.ijheatmasstransfer.2018.05.105.

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20

Barbosa,, Jader R., and Geoffrey F. Hewitt. "A Thermodynamic Nonequilibrium Slug Flow Model." Journal of Heat Transfer 127, no. 3 (March 1, 2005): 323–31. http://dx.doi.org/10.1115/1.1857945.

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This paper presents a calculation methodology to predict the peaks in heat transfer coefficient at near zero equilibrium quality observed in forced convective boiling in vertical conduits. The occurrence of such peaks is typical of low latent heat, low thermal conductivity systems (such as refrigerants and hydrocarbons), and of systems in which the vapor volume formation rate for a given heat flux is large (low-pressure water). The methodology is based on a model that postulates that the mechanism behind the heat transfer coefficient enhancement is the existence of thermodynamic nonequilibrium slug flow, i.e., a type of slug flow in which rapid bubble growth in subcooled boiling leads to the formation of Taylor bubbles separated by slugs of subcooled liquid. Results are compared with experimental data for forced convective boiling of pure hydrocarbons and show considerable improvement over existing correlations.

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21

Delhaye, Jean-Marc. "SOME ISSUES RELATED TO THE MICROPHYSICS OF FORCED CONVECTIVE BOILING." Multiphase Science and Technology 15, no. 1-4 (2003): 373–75. http://dx.doi.org/10.1615/multscientechn.v15.i1-4.310.

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22

INABA, Noriaki. "Visualization of bubble behaviors in forced convective subcooled flow boiling." Journal of the Visualization Society of Japan 28-1, no. 1 (2008): 405. http://dx.doi.org/10.3154/jvs.28.405.

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23

KAWANAMI, Osamu, Teruo NISHIDA, Itsuro HONDA, Yousuke KAWASHIMA, and Haruhiko OHTA. "The Effect of Gravitational Orientation on Cryogenic Forced Convective Boiling." Progress in Multiphase Flow Research 2 (2007): 109–16. http://dx.doi.org/10.3811/pmfr.2.109.

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24

Yen, Tzu-Hsiang, Hiroki Nasu, Nobuhide Kasagi, and Yuji Suzuki. "G211 Forced Convective Boiling Heat Transfer in a Micro Tube." Proceedings of thermal engineering conference 2001 (2001): 625–26. http://dx.doi.org/10.1299/jsmeptec.2001.0_625.

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25

Jensen, M. K., and H. P. Bensler. "Saturated Forced-Convective Boiling Heat Transfer With Twisted-Tape Inserts." Journal of Heat Transfer 108, no. 1 (February 1, 1986): 93–99. http://dx.doi.org/10.1115/1.3246910.

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26

SUZUKI, Shinju, and Satoshi KUMAGAI. "Subcooled Forced-Convective Boiling Heat Transfer with Twisted Tape Inserts." Transactions of the Japan Society of Mechanical Engineers Series B 62, no. 598 (1996): 2356–62. http://dx.doi.org/10.1299/kikaib.62.2356.

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27

OKAWA, Tomio, Tatsuhiro ISHIDA, Isao KATAOKA, and Michitsugu MORI. "3519 A Visual Study of Forced-Convective Subcooled Flow Boiling." Proceedings of the JSME annual meeting 2005.3 (2005): 195–96. http://dx.doi.org/10.1299/jsmemecjo.2005.3.0_195.

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28

Situ, Rong, Takashi Hibiki, Mamoru Ishii, and Michitsugu Mori. "Bubble lift-off size in forced convective subcooled boiling flow." International Journal of Heat and Mass Transfer 48, no. 25-26 (December 2005): 5536–48. http://dx.doi.org/10.1016/j.ijheatmasstransfer.2005.06.031.

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29

Cao, Yang, Zensaku Kawara, Takehiko Yokomine, and Tomoaki Kunugi. "ICONE23-1761 AN EXPERIMENTAL STUDY ON BUBBLE BEHAVIORS IN FORCED CONVECTIVE SUBCOOLED BOILING OF HIGH SUBCOOLINGS." Proceedings of the International Conference on Nuclear Engineering (ICONE) 2015.23 (2015): _ICONE23–1—_ICONE23–1. http://dx.doi.org/10.1299/jsmeicone.2015.23._icone23-1_372.

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30

Pasamehmetoglu, K. O., R. A. Nelson, and F. S. Gunnerson. "Critical Heat Flux Modeling in Forced Convection Boiling During Power Transients." Journal of Heat Transfer 112, no. 4 (November 1, 1990): 1058–62. http://dx.doi.org/10.1115/1.2910478.

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In this paper, a theoretical prediction of critical heat flux (CHF) during power transients in forced convective boiling is presented. The analysis is restricted to departure from nucleate boiling (DNB) type of CHF at low qualities. The developed theory is compared with the experimental data available in the literature. The agreement is exceptionally good. The new model also is compared with the semi-empirical transient CHF model in the literature.

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31

Sarafraz, Mohammad Mohsen, and Faramarz Hormozi. "Forced Convective and Nucleate Flow Boiling Heat Transfer to Alumnia Nanofluids." Periodica Polytechnica Chemical Engineering 58, no. 1 (2014): 37. http://dx.doi.org/10.3311/ppch.2206.

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32

Murata, Keiji, Keisuke Okamoto, and Koichi Araga. "H114 Forced Convective Boiling of Refrigerant HCFC123 in a Mini-Tube." Proceedings of the Thermal Engineering Conference 2010 (2010): 215–16. http://dx.doi.org/10.1299/jsmeted.2010.215.

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33

STANGL, G., and F. MAYINGER. "VOID FRACTION MEASUREMENT IN SUBCOOLED FORCED CONVECTIVE BOILING WITH REFRIGERANT 12." Experimental Heat Transfer 3, no. 3 (September 1990): 323–40. http://dx.doi.org/10.1080/08916159008946393.

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34

AKHANDAI, M. A. R., and D. D. JAMES. "RIB ORIENTATION EFFECTS ON HEAT TRANSFER PERFORMANCE IN FORCED CONVECTIVE BOILING." Chemical Engineering Communications 139, no. 1 (July 1995): 15–24. http://dx.doi.org/10.1080/00986449508936395.

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35

ISHIGAKI, Hideyuki, and Yuichi FUNAWATASHI. "J0103-4-4 Forced Convective Boiling Heat Transfer in Micro Channels." Proceedings of the JSME annual meeting 2009.6 (2009): 75–76. http://dx.doi.org/10.1299/jsmemecjo.2009.6.0_75.

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36

MURATA, Keiji, Masahito OHNARU, Ryota HAYAMI, and Koichi ARAGA. "D222 Forced convective boiling of refrigerant HCFC123 in a mini-tube." Proceedings of the Thermal Engineering Conference 2007 (2007): 295–96. http://dx.doi.org/10.1299/jsmeted.2007.295.

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37

Celata, GianPiero, and Maurizio Cumo. "A review of pool and forced convective boiling of binary mixtures." Experimental Thermal and Fluid Science 7, no. 2 (August 1993): 129. http://dx.doi.org/10.1016/0894-1777(93)90108-u.

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38

Celata, G. P., M. Cumo, and T. Setaro. "A review of pool and forced convective boiling of binary mixtures." Experimental Thermal and Fluid Science 9, no. 4 (November 1994): 367–81. http://dx.doi.org/10.1016/0894-1777(94)90015-9.

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39

Huang, Jen-Hung, Wei-Hung Shih, Wen-Hsin Hsieh, and Shaw-Ruey Lyu. "109. Cooling rate and cryoprotectant concentration in forced-convective-boiling vitrification." Cryobiology 63, no. 3 (December 2011): 336. http://dx.doi.org/10.1016/j.cryobiol.2011.09.112.

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40

NISHIMURA, Yusuke, Junnosuke OKAJIMA, Takuya OOUCHI, and Atsuki KOMIYA. "Evaluation of forced convective boiling heat transfer with layered parallel microchannels." Journal of Thermal Science and Technology 15, no. 1 (2020): JTST0006. http://dx.doi.org/10.1299/jtst.2020jtst0006.

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41

MURATA, Keiji, Ryota HAYAMI, and Koichi ARAGA. "408 Forced convective boiling of refrigerant HCFC123 in a mini-tube." Proceedings of Conference of Tokai Branch 2008.57 (2008): 273–74. http://dx.doi.org/10.1299/jsmetokai.2008.57.273.

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42

MURATA, Keiji, Takuya MIKI, Keisuke OKAMOTO, Kazuhisa YABUKI, and Koichi ARAGA. "651 Forced convective boiling of refrigerant HCFC123 in a mini-tube." Proceedings of Conference of Tokai Branch 2009.58 (2009): 391–92. http://dx.doi.org/10.1299/jsmetokai.2009.58.391.

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43

Sami, S. M., and J. Schnotale. "Forced convective boiling of nonazeotropic refrigerant mixtures inside enhanced surface tubing." International Journal of Energy Research 16, no. 7 (September 1992): 637–51. http://dx.doi.org/10.1002/er.4440160706.

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44

Pamitran, A. S., Kwang-Il Choi, Jong-Taek Oh, and Hoo-Kyu Oh. "Forced convective boiling heat transfer of R-410A in horizontal minichannels." International Journal of Refrigeration 30, no. 1 (January 2007): 155–65. http://dx.doi.org/10.1016/j.ijrefrig.2006.06.005.

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45

Caira, M., E. Cipollone, M. Cumo, and A. Naviglio. "Forced convective boiling in high pressure parallel flow in tube bundles." Nuclear Engineering and Design 99 (February 1987): 25–29. http://dx.doi.org/10.1016/0029-5493(87)90104-x.

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46

Suzuki, Shinju, and Satoshi Kumagai. "Transient behavior of subcooled forced-convective boiling with twisted tape inserts." Heat Transfer - Japanese Research 25, no. 3 (1996): 178–91. http://dx.doi.org/10.1002/(sici)1520-6556(1996)25:3<178::aid-htj4>3.0.co;2-u.

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47

Azadbakhti, Reza, Farzad Pourfattah, Abolfazl Ahmadi, Omid Ali Akbari, and Davood Toghraie. "Eulerian–Eulerian multi-phase RPI modeling of turbulent forced convective of boiling flow inside the tube with porous medium." International Journal of Numerical Methods for Heat & Fluid Flow 30, no. 5 (July 17, 2019): 2739–57. http://dx.doi.org/10.1108/hff-03-2019-0194.

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Purpose The purpose of this study is simulation the flow boiling inside a tube in the turbulent flow regime for investigating the effect of using a porous medium in the boiling procedure. Design/methodology/approach To ensure the accuracy of the obtained numerical results, the presented results have been compared with the experimental results, and proper coincidence has been achieved. In this study, the phase change phenomenon of boiling has been modeled by using the Eulerian–Eulerian multi-phase Rensselaer Polytechnic Institute (RPI) wall boiling model. Findings The obtained results indicate using a porous medium in boiling process is very effective in a way that by using a porous medium inside the tub, the location of changing the liquid to the vapor and the creation of bubbles, changes. By increasing the thermal conductivity of porous medium, the onset of phase changing postpones, which causes the enhancement of heat transfer from the wall to the fluid. Generally, it can be said that using a porous medium in boiling flows, especially in flow with high Reynolds numbers, has a positive effect on heat transfer enhancement. Also, the obtained results revealed that by increasing Reynolds number, the created vapor phase along the tube decreases and by increasing Reynolds number, the Nusselt number enhances. Originality/value In present research, by using the computational fluid dynamics, the effect of using a porous medium in the forced boiling of water flow inside a tube has been investigated. The fluid boiling inside the tube has been simulated by using the multi-phase Eulerian RPI wall boiling model, and the effect of thermal conductivity of a porous medium and the Reynolds number on the flow properties, heat transfer and boiling procedure have been investigated.

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48

Finlay, I. C., D. Harris, D. J. Boam, and B. I. Parks. "Factors Influencing Combustion Chamber Wall Temperatures in a Liquid-Cooled, Automotive, Spark-Ignition Engine." Proceedings of the Institution of Mechanical Engineers, Part D: Transport Engineering 199, no. 3 (July 1985): 207–14. http://dx.doi.org/10.1243/pime_proc_1985_199_158_01.

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The influence on cylinder head temperatures of parameters such as cylinder head material, coolant composition, pressure, temperature and velocity was investigated. Each of these parameters was systematically varied and its influence on combustion chamber wall temperature measured. Good agreement is shown between the measured values and corresponding predictions from a heat transfer model incorporating forced-convective, sub-cooled, nucleate boiling. The results suggest that nucleate boiling can play an important role in the transfer of heat from cylinder head to coolant.

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49

Murata, Keiji, Keisuke Okamoto, Tomoaki Ishida, Yuhki Ochi, and Koichi Araga. "F213 Forced convective boiling of a refrigerant HCFC123 in a mini-tube." Proceedings of the Thermal Engineering Conference 2009 (2009): 279–80. http://dx.doi.org/10.1299/jsmeted.2009.279.

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50

Murano, Toru, Satoshi Matsumoto, Akiko Kaneko, Yutaka Abe, Kenichiro Sawada, Osamu Kawanami, Hitoshi Asano, and Haruhiko Ohta. "Effect of Non-Condensable Gas on Bubble Formation in Forced Convective Boiling." Proceedings of the Thermal Engineering Conference 2018 (2018): 0155. http://dx.doi.org/10.1299/jsmeted.2018.0155.

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