Abdelall, F., Hahn, G., Ghiaasiaan, S. M., Abdel-Khalik, S. I., Jeter, S. M., Yoda, M., and Sadowski, D. L. (2005). Pressure drop caused by abrupt flow area changes in microchannels, Exp. Thermal Fluid Sci., 29, 425–434, 2005.CrossRefGoogle Scholar

Abdollahian, D., Chexal, B., and Norris, D. M. (1983). Prediction of leak rates through intergranular stress corrosion cracks. Proc. CSNI Leak-Before-Break Conf., Nuclear Regulatory Commission Rep. NUREG/CP-00151, pp. 300–326.Google Scholar

Abdollahian, D., Healzer, J., Janssen, E., and Amos, C. (1982). Critical flow data review and analysis. Electric Power Research Institute Rep. EPRI NP-2192, Palo Alto, CA.Google Scholar

Abe, Y., Oka, T., Mori, Y., and Negashima, A. (1994). Pool boiling of a non-azeotropic mixture under microgravity. Int. J. Heat Mass Transfer, 37, 2405–2413.CrossRefGoogle Scholar

Ackerman, G. (1937). Heat transfer and molecular mass transfer in the same field at high temperatures and large partial pressure differences. Forsch. Ing. Wes., VDI, Forschungesheft, 8, 232.Google Scholar

Acosta, R. E., Buller, R. H., and Tobias, C. W. (1985). Transport processes in narrow (capillary) channels. AIChE J., 81, 473–482.CrossRefGoogle Scholar

Adams, T. M., Abdel-Khalik, S. I., Jeter, S. M., and Qureshi, Z. H. (1997). An experimental investigation of single-phase forced convection in microchannels. Int. J. Heat Mass Transfer, 41, 851–857.CrossRefGoogle Scholar

Adams, T. M., Ghiaasiaan, S. M., and Abdel-Khalik, S. I. (1999). Enhancement of liquid forced convection heat transfer in microchannels due to the release of dissolved noncondensables. Int. J. Heat Mass Transfer, 42, 3563–3573.CrossRefGoogle Scholar

Agarwal, A. (2006). Heat transfer and pressure drop during condensation of refrigerants in microchannels. Pressure (N/m2); Legendre polynomialh.D. thesis, Georgia Institute of Technology, Atlanta.Google Scholar

Agostini, B., and Bontemps, A. (2005). Vertical flow boiling of refrigerant R134a in small channels. Int. J. Heat Mass Transfer, 26, 296–306.Google Scholar

Ahmad, S. Y. (1970). Axial distribution of bulk temperature and void fraction in a heated channel with inlet subcooling. Int. J. Heat Mass Transfer, 92, 595–609.Google Scholar

Ahmand, S. Y. (1973). Fluid to fluid modeling of critical heat flux: A compensated distortions model. Int. J. Heat Mass Transfer, 16, 641–662.CrossRefGoogle Scholar

Akbar, M. K., and Ghiaasiaan, S. M. (2006). Simulation of Taylor flow in capillaries based on the volume-of-fluid Technique, Ind. Eng. Chem. Res., 45, 5396–5403, 2006.CrossRefGoogle Scholar

Akbar, M. K., Plummer, D. A., and Ghiaasiaan, S. M. (2003). On gas–liquid two-phase flow regimes in microchannels. Int. J. Multiphase Flow, 29, 855–865.CrossRefGoogle Scholar

Akers, W. W., Deans, H. A., and Crosser, O. K. (1959). Condensation heat transfer within horizontal tube. Chem. Eng. Prog. Symp. Ser., 55, 171–176.Google Scholar

Alamgir, M. D., and Lienhard, J. H. (1981). Correlation of pressure undershoot during hot-water depressurization. J. Heat Transfer, 103, 52–55.CrossRefGoogle Scholar

Al-Diwani, H. K., and Rose, J. W. (1973). Free convection film condensation of steam in the presence of noncondensing gases. Int. J. Heat Mass Transfer, 16, 1359–1369.CrossRefGoogle Scholar

Alekseev, V. P., Poberezkin, A. E., and Gerasimov, P. V. (1972). Determination of flooding rates in regular packings. Heat Transfer Sov. Res., 4(6), 159–163.Google Scholar

Al-Hayes, R. A. M., and Winterton, R. H. S. (1981). Bubble diameter on detachment in flowing liquids. Int. J. Heat Mass Transfer, 24, 223–230.CrossRefGoogle Scholar

Ali, M. I., and Kawaji, M. (1991). The effect of flow channel orientation on two-phase flow in a narrow passage between flat plates. Proc., ASME/JSME Thermal Eng. Conf., 2, 183– 190.Google Scholar

Ali, M. I., Sadatomi, M., and Kawaji, M. (1993). Adiabatic two-phase flow in narrow channels between two flat plates. Can. J. Chem. Eng., 71, 657–666.CrossRefGoogle Scholar

Alopaeus, V., Koshinen, J., and Keskinen, K. I. (1999). Simulation of the population balances for liquid-liquid systems in a nonideal stirred tank. Part 1: Description and qualitative validation of the model. Chem. Eng. Sci., 54, 5887–5899.CrossRefGoogle Scholar

Aly, M. M. (1981). Flow regime boundaries for an interior subchannel of a horizontal 37 element bundle. Can J. Chem. Eng., 59, 158–163.CrossRefGoogle Scholar

Amos, C. N., and Schrock, V. E. (1984). Two-phase critical flow in slits. Nucl. Sci. Eng., 88, 261–274.CrossRefGoogle Scholar

Andresen, U. (2007). Supercritical gas cooling and near-critical-pressure condensation of refrigerant blends in microchannels. Pressure (N/m2); Legendre polynomial Homogeneous Tube or jet diameter (m) Thesis, Georgia Institute of Technology, Atlanta, GA.

Ansari, M. R., and Nariai, H. (1989). Experimental investigation on wave initiation and slugging of air-water stratified flow in horizontal duct. J. Nucl. Sci. Technol., 26, 681–688.CrossRefGoogle Scholar

Antal, S. P., Lahey, R. T. Jr., and Flaherty, J. E. (1991). Analysis of phase distribution in fully developed laminar bubbly two-phase flow. Int. J. Multiphase Flow, 17, 635–652.CrossRefGoogle Scholar

Ardron, K. H. (1978). A two-fluid model for critical vapor-liquid flow. Int. J. Multiphase Flow, 4, 323–327.CrossRefGoogle Scholar

Armand, A. A. (1959). The resistance during the movement of a two-phase system in horizontal pipes. Atomic Energy Research Establishment (AERE) Libr. Trans. 828.Google Scholar

Asali, J. C., Hanratty, T. J., and Andreussi, P. (1985). Interfacial drag and film height for vertical annular flow. AIC Homogeneous E J., 31, 895–902.CrossRefGoogle Scholar

Aussillous, P., and Quéré, D. (2000). Quick deposition of a fluid on the wall of a tube. Phys. Fluids, 12, 2367–2371.CrossRefGoogle Scholar

Azer, N. H., and Said, S. A. (1986). Heat transfer analysis of annular flow condensation inside circular and semi-circular horizontal tubes. ASHRAE Trans., 92, 41–54.Google Scholar

Baker, O. (1954). Simultaneous flow of oil and gas. Oil Gas J., 53, 185–195.Google Scholar

Bailey, N. A. (1971). Film boiling on submerged vertical cylinders. AEEW-M1051.

Baird, J. R., Fletcher, D. F., and Haynes, B. S. (2003). Local condensation heat transfer in fine passages. Int. J. Heat Mass Transfer, 46, 4453–4466.CrossRefGoogle Scholar

Banerjee, S. (1980). Analysis of separated flow models. Electric Power Research Institute Rep. EPRI NP-1442, Palo Alto, CA.Google Scholar

Banerjee, S. B., and Chan, A. M. (1980). Separated flow models – I Analysis of the average and local instantaneous formulations. Int. J. Multiphase Flow, 6, 1–24.CrossRefGoogle Scholar

Bankoff, S. G. (1963). Asymptotic growth of a bubble in a liquid with uniform initial superheat. Appl. Sci. Res., 12A, 567.Google Scholar

Bankoff, S. G., and Lee, S. C. (1986). A critical review of the flooding literature. In Multiphase Science and Technology, Hewitt, G. F., Delhaye, J. M., and Zuber, N., Eds., Hemisphere, New York, Vol. 2, Chapter 2.CrossRefGoogle Scholar

Bankoff, S. G., and Lee, S. C. (1987). Flooding and hysteresis effects in nearly-horizontal countercurrent stratified stead-water flow. Int. J. Heat Mass Transfer, 30, 581–588.CrossRefGoogle Scholar

Bankoff, S. G., Tankin, R. S., Yuen, M. C., and Hsieh, C. L. (1981). Countercurrent flow of air/water and steam/water through a horizontal perforated plate. Int. J. Heat Mass Transfer, 24, 1381–1395.CrossRefGoogle Scholar

Bao, Z.-Y., Bosnich, M. G., and Haynes, B. S. (1994). Estimation of void fraction and pressure drop for two-phase flow in fine passages. Trans. Inst. Chem. Eng., 72A, 625–532.Google Scholar

Bao, Z. Y., Fletcher, D. F., and Haynes, B. S. (2000). Flow boiling heat transfer of Freon R11 and HCFC123 in narrow passages. Int. J. Heat Mass Transfer, 43, 3347–3358.CrossRefGoogle Scholar

Bapat, P. M., and Tavralides, L. L. (1985). Mass transfer in a liquid-liquid CFSTR, AIC Homogeneous E J., 31, 659–666.CrossRefGoogle Scholar

Barajas, A. M., and Panton, R. L. (1993). The effect of contact angle on two-phase flow in capillary tubes. Int. J. Multiphase Flow, 19, 337–346.CrossRefGoogle Scholar

Barnea, D. (1986). Transition from annular and from dispersed bubble flow – Unified models for the whole range of pipe inclination. Int. J. Multiphase Flow, 12, 733–744.CrossRefGoogle Scholar

Barnea, D. (1987). A unified model for predicting flow-pattern transitions for the whole range of pipe inclinations. Int. J. Multiphase Flow, 13, 1–12.CrossRefGoogle Scholar

Barnea, D., Yoseph, Ben N., and Taitel, Y. (1986). Flooding in inclined pipes – Effects of entrance section. Can. J. Chem. Eng., 64, 177–184.CrossRefGoogle Scholar

Barnea, D.Lulinkski, Y., and Taitel, Y. (1983). Flow in small diameter pipes. Can. J. Chem. Eng., 61, 617–620.CrossRefGoogle Scholar

Barnea, D., Shoham, O., and Taitel, Y. (1982). Flow pattern transition for vertical downward two-phase flow. Chem. Eng. Sci., 37, 741–744.CrossRefGoogle Scholar

Barnea, D., Shoham, O., and Taitel, Y. (1985). Gas-liquid flow in inclined tubes: Flow pattern transitions for upward flow. Chem. Eng. Sci., 40, 131–136.CrossRefGoogle Scholar

Baroczy, C. J. (1963). Correlation of liquid fraction in two-phase flow with application to liquid metals. NAA-SR-8171.CrossRef

Basu, N., Warrier, G. R., and Dhir, V. K. (2002). Onset of nucleate boiling and active nucleation site density during subcooled flow boiling. J. Heat Transfer, 124, 717–728.CrossRefGoogle Scholar

Batchelor, G. K. (1970). Theory of Homogeneous Turbulence, Cambridge University Press, Cambridge.Google Scholar

Baumeister, K. J., and Simon, F. F. (1973). Leidenfrost temperature – Its correlation for liquid metals, cryogens, hydrocarbons, and water. J. Heat Transfer, 95, 166–173.CrossRefGoogle Scholar

Beattie, D. R. H. (1973). A note on the calculation of two-phase pressure losses. Nucl. Eng. Design, 25, 395–402.CrossRefGoogle Scholar

Beattie, D. R. H., and Whalley, P. B. (1982). A simple two-phase frictional pressure drop calculation method. Int. J. Multiphase Flow, 8, 83–87.CrossRefGoogle Scholar

Becker, K. M. (1971). Measurement of burnout conditions for flow of boiling water in horizontal round tubes. Rep. No. AERL-1262, Atomenergia-Aktieb, Sweden.Google Scholar

Benedek, S. (1976). Heat transfer at the condensation of steam on turbulent water jet. Int. J. Heat Mass Transfer, 19, 448–450.CrossRefGoogle Scholar

Benjamin, T. B. (1957). Wave formation in laminar flow down an inclined plane. J. Fluid Mech., 2, 554–574.CrossRefGoogle Scholar

Bennett, D. L., and Chen, J. C. (1980). Forced convective boiling in vertical tubes for saturated pure components and binary mixtures. AIC Homogeneous E J., 24, 223–230.Google Scholar

Bennett, M. K., and Rohani, S. (2001). Solution of polulation balance equations with a new combined Lax–Wendroff/Cranck–Nicholson method. Chem. Eng. Sci., 56, 6623–6633.CrossRefGoogle Scholar

Bennett, J. A. R., Collier, J. G., Pratt, H. R. C., and Thornton, D. (1961). Heat transfer to two-phase gas-liquid systems. Steam-water mixtures in the liquid-dispersed region in an annulus. Trans. Inst. Chem. Eng., 39, 113–126.Google Scholar

Bercic, G., and Pintar, A. (1997). The role of gas bubbles and liquid slug lengths on mass transport in the taylor flow through capillaries. Chem. Eng. Sci., 52, 3709–3719.Google Scholar

Berenson, P. J. (1961). Film-boiling heat transfer from a horizontal surface. J. Heat Transfer, 83, 351–358.CrossRefGoogle Scholar

Bergles, A. E. (1962). Subcooled burnout in tubes of small diameter. ASME Paper 63-WA-182.

Bergles, A. E. (1978). Instabilities in two-phase flow. In Two-Phase Flow and Heat Transfer in Power and Process Industries, Bergles, A. E., Collier, J. G., Delhaye, J. M., Hewitt, G. F., and Mayinger, F., Eds., Hemisphere, Washington, Direct-contact.Google Scholar

Bergles, A. E., and Kandlikar, S. G. (2005). On the nature of critical heat flux in microchannels. J. Heat Transfer, 127, 101–107.CrossRefGoogle Scholar

Bergles, A. E., and Rohsenow, W. M. (1964). The determination of forced convection surface boiling heat transfer. Int. J. Heat Mass Transfer, 86, 365–372.Google Scholar

Berman, L. D., and Fuks, S. N. (1958). Mass transfer in condensers with horizontal tubes when the steam contains air. Teploenergetika, 5(8), 66–74.Google Scholar

Bertoletti, S., Gaspari, G. P., Lombardi, C., Peterlongo, G., Silvestri, M., and Tacconi, F. A. (1965). Heat transfer crisis with steam water mixtures. Energia Nucleare, 12, 121–172.Google Scholar

Bharathan, D., and Wallis, G. B. (1983). Air-water countercurrent annular flow. Int. J. Multiphase Flow, 9, 349–366.CrossRefGoogle Scholar

Bharathan, D., Wallis, G. B., and Richter, H. J. (1979). Air-water countercurrent annular flow. Electric Power Research Institute Rep. EPRI NP-1165, Palo Alto, CA.Google Scholar

Bibeau, E. L., and Salcudean, M. (1990). The effect of flow direction on void growth at very low velocities and low pressure. Int. Comm. Heat Mass Transfer, 17, 19–25.CrossRefGoogle Scholar

Bibeau, E. L., and Salcudean, M. (1994a). Subcooled voidage growth mechanisms and prediction at low pressure and low velocity. Int. J. Multiphase Flow, 20, 837–863.CrossRefGoogle Scholar

Bibeau, E. L., and Salcudean, M. (1994b). A study of bubble ebullition in forced-convective subcooled nucleate boiling at low pressure. Int. J. Heat Mass Transfer, 37, 2245–2259.CrossRefGoogle Scholar

Binnie, A. M. (1957). Experiments on the onset of wave formation on a film of water flowing down a vertical plate. J. Fluid Mech., 2, 551–553.CrossRefGoogle Scholar

Bird, R. B., Stewart, W. E., and Lightfoot, E. N. (2002). Transport Phenomena, 2nd ed., Wiley, New York.Google Scholar

Birkhoff, G., Margulies, R. S., and Horning, W. A. (1958). Spherical bubble growth. Phys. Fluids, 1, 201.CrossRefGoogle Scholar

Bjonard, T. A., and Griffith, P. (1977). Pressurized water reactor blowdown heat transfer. In Symposium on Thermal and Hydraulic Aspects of Nuclear Reactor Safety, Jones, O. C., and Bankoff, S. G., Eds., ASME, New York, Vol. 1.Google Scholar

Bjorge, R. W., Hall, G. R., and Rohsenow, W. M. (1982). Correlation of forced convection boiling heat transfer data. Int. J. Heat Mass Transfer, 25, 753–757.CrossRefGoogle Scholar

Blasick, A. M., Dowling, M. F., Abdel-Khalik, S. I., Ghiaasiaan, S. M., and Jeter, S. M. (2002). Onset of flow instability in uniformly-heated thin horizontal annuli. Exp. Thermal Fluid Sci., 26, 1–14.Google Scholar

Blinkov, V. N., Jones, O. C., Jr. and Nigmatulin, B. I. (1993). Nucleation and flashing in nozzles – 2 Comparison with experiments using a five-equation model for vapor void development. Int. J. Multiphase Flow, 19, 965–986.CrossRefGoogle Scholar

Block, J. A., and Crowley, C. J. (1976). Effect of steam upflow and superheated walls on ECC delivery in a simulated multiloop Pressurized water reactor geometry. CREARE Rep. TN-2110, Creare, NH.Google Scholar

Bolstad, M. M., and Jordan, R. C. (1948). Theory and use of the capillary tube expansion device. Refrig. Eng., 56, 519.Google Scholar

Bonjour, J., and Lallemand, M. (1998). Flow patterns during boiling in a narrow space between two vertical surfaces. Int. J. Multiphase Flow, 24, 947–960.CrossRefGoogle Scholar

Borishanskiy, V. M., et al. (1977). Effect of uncondensable gas content on heat transfer in steam condensation in a vertical tube. Heat Transfer Sov. Res., 9(2), 2, 35–42.Google Scholar

Borishanskiy, V. M., et al. (1978). Heat transfer from steam condensing inside vertical pipes and coils. Heat Transfer Sov. Res., 10(4), 44–58.Google Scholar

Bose, F., Ghiaasiaan, S. M., and Heindel, T. J. (1997). Hydrodynamics of dispersed liquid droplets in agitated synthetic fibrous slurries. Ind. Eng. Chem. Res., 36, 5028–5039.CrossRefGoogle Scholar

Bouré, J. A. (1977). The critical flow phenomena with reference to two-phase flow and nuclear reactor systems. Proc., ASME Symp. Thermal-Hydraulic Aspects of Nuclear Reactor Safety, ASME, New York, pp. 195–216.Google Scholar

Bouré, J. A., and Delhaye, J. M. (1981). Chapter 12. In Thermohydraulics of Two-Phase Systems for Industrial Design and Nuclear Engineering, Delhaye, , Giot, M., Riethermuller, M., , L. M., Eds., Hemisphere, Washington, Direct-contact, pp. 353–403.Google Scholar

Bouré, J. A., Bergles, A. E., and Tong, L. S. (1973). Review of two-phase flow instability. Nucl. Eng. Design, 25, 165–192.CrossRefGoogle Scholar

Bousman, W. S., McQuillen, J. B., and Witte, L. C. (1996). Gas-liquid flow patterns in microgravity: Effects of tube diameter, liquid viscosity and surface tension. Int. J. Multiphase Flow, 22, 1035–1053.CrossRefGoogle Scholar

Bowers, M. B., and Mudawar, I. (1994). High flux boiling in low flow rate, low pressure drop mini-channel and micro-channel heat sinks. Int. J. Heat Mass Transfer, 37, 321–332.CrossRefGoogle Scholar

Bowring, R. W. (1972). A simple but accurate round tube, uniform heat flux, dryout correlation over the pressure range 0.7–17 MN/m2 (100–2500 psia). UKAEA Rep. AEEW-R789, Winfrith, England.

Bowring, R. W. (1979). WSC-2: A subcooled dryout correlation for water-cooled clusters over the pressure range 3.4–15.9 MPa (500–2300 PSIA). UKAEA Rep. AEEW–R983, Winfrith, England.

Bowring, R. W. (1962). Physical model of bubble detachment and void volume in subcooled boiling. OECD Halden Reactor Project Rep. HPR-10.

Boyd, R. D. (1985a). Subcooled flow boiling critical heat flux (Critical heat flux) and its application to fusion energy components. Part I. A review of fundamentals of Critical heat flux and related data base. Fusion Technol. 7, 1–30.CrossRefGoogle Scholar

Boyd, R. D. (1985b). Subcooled flow boiling critical heat flux (Critical heat flux) and its application to fusion energy components. Part II. A review of microconvective, experimental, and correlational aspects. Fusion Technol. 7, 31–52.CrossRefGoogle Scholar

Boyd, R. D. (1988). Subcooled water flow boiling experiments under uniform high heat flux conditions. Fusion Technol. 13, 131–142.CrossRefGoogle Scholar

Boyd, R. D. (1990). Subcooled water flow boiling transition and the L/D effect on Critical heat flux for a horizontal uniformly heated tube. Fusion Technol. 18, 317–324.CrossRefGoogle Scholar

Brauer, H. (1956). Strömung und Wärmeübertragung bei Rieselfilmen. VDI-Verlag, Düsseldorf, p. 457.Google Scholar

Braum, B., Ikier, C., and Klein, H. (1993). Thermocapillary migration of droplets in a binary mixture with miscibility gap during liquid, liquid phase separation under reduced gravity. J. Colloid Interface Sci., 159, 515–516.CrossRef

Brauner, N., and Moalem-Maron, D. (1992). Identification of the range of ‘small diameter’ conduits, regarding two-phase flow pattern transitions. Int. Comm. Heat Mass Transfer, 19, 29–39.CrossRefGoogle Scholar

Brauner, N., and Maron, Molem D. (1982). Characteristics of inclined thin films, waviness and the associated mass transfer. Int. J. Heat Mass Transfer, 25, 99–110.CrossRefGoogle Scholar

Brauner, N., and Maron, Molem D. (1983). Modeling of wavy flow in inclined thin films. Chem. Eng. Sci., 38, 775–788.CrossRefGoogle Scholar

Breber, D., Palen, J. W., and Taborek, J. (1980). Prediction of horizontal tubeside condensation of pure components using flow regime criteria. J. Heat Transfer, 102, 471–476.CrossRefGoogle Scholar

Breen, B. P., and Westwater, J. W. (1962). Effect of diameter of horizontal tubes on film boiling heat transfer. Chem. Eng. Prog., 58(7), 67.Google Scholar

Bretherton, F. B. (1961). The motion of long bubbles in tubes. J. Fluid Mech. 10, Part 2, 166–188.CrossRefGoogle Scholar

Brodkey, R. S. (1967). The Phenomena of Fluid Motion, Addison-Wesley, Reading, MA.Google Scholar

Bromley, L. A. (1950). Heat transfer in stable film boiling. Chem. Eng. Prog. Symp. Ser. 46, 221–227.Google Scholar

Brotz, W. (1954). Uber die vorausberechnung der absorptions geschwindigwert von gasen in stramen der fussigkeitschichten. Chem. Eng. Technol. 26, 470–478.Google Scholar

Brouwers, H. J. H. (1991). An improved tangency condition for fog formation in cooler-condensers. Chem. Eng. Sci., 47, 3023–3036.CrossRefGoogle Scholar

Brouwers, H. J. H. (1992). A film model for heat and mass transfer with fog formation. Int. J. Heat Mass Transfer, 34, 2387–2394.CrossRefGoogle Scholar

Brouwers, H. J. H. (1996). Effect of fog formation on turbulent vapor condensation with noncondensable gases. J. Heat Transfer, 118, 243–245.CrossRefGoogle Scholar

Brutin, D., Topin, F., and Tadris, L. (2003). Experimental study of convective boiling in heated minichannels. Int. J. Heat Mass Transfer, 46, 2957–2965.CrossRefGoogle Scholar

Brutin, D., Topin, F., and Tadris, L. (2004). Pressure drop and heat transfer analysis of flow boiling in a minichannel: Influence of the inlet condition on two-phase flow stability. Int. J. Heat Mass Transfer, 47, 2365–2377.CrossRefGoogle Scholar

Bui, T. D., and Dhir, V. K. (1985). Transition boiling heat transfer on a vertical surface. J. Heat Transfer, 107, 756–763.CrossRefGoogle Scholar

Butterworth, D. (1975). A comparison of some void-fraction relationships for co-current gas-liquid flow. Int. J. Multiphase Flow, 1, 845–850.CrossRefGoogle Scholar

Butterworth, D. (1988). Condensers and their design. In Two-Phase Flow Heat Exchangers, Kakac, S., Bergles, A. E., and Fernandes, Oliveira E., Eds., Kluwer, Dordrecht, pp. 779–828.CrossRefGoogle Scholar

Caira, M., Caruso, G., and Naviglio, A. (1995). A correlation to predict Critical heat flux in subcooled flow boiling. Int. Comm. Heat Mass Transfer, 22, 35–45.CrossRefGoogle Scholar

Calderbank, P. H., and Korchinski, I. J. O. (1956). Circulation in liquid drops. Chem. Eng. Sci., 6, 65–78.CrossRefGoogle Scholar

Cammenga, H. K., Schulze, F. W., and Theuerl, W. (1977). Vapor pressure and evaporation coefficient of water. J. Chem Eng. Data, 22, 131–134.CrossRefGoogle Scholar

Camp, D. W., and Berg, J. C. (1987). The spreading of oil on water in surface-tension regime. J. Fluid Mech., 184, 445–462.CrossRefGoogle Scholar

Carey, V. P. (1992). Liquid–Vapor Phase-Change Phenomena, Hemisphere, Washington, Direct-contact.Google Scholar

Carey, V. P (1999). Statistical Thermodynamics and Microscale Thermophysics, Cambridge University Press, Cambridge.CrossRefGoogle Scholar

Catton, I., Ghiaasiaan, S. M., and Duffey, R. B. (1988). Multi-dimensional thermal-hydraulics and two-phase phenomena during quenching of hot rod bundles. In Transient Phenomena in Multiphase Flow, Afgan, N. H., Ed., Hemisphere, Washington Direct-contact, pp. 491–525.Google Scholar

Cavallini, A., Censi, G., Col, Del D., Doretti, L., Longo, G. A., and Rossetto, L. (2001). Experimental investigation on condensation of new HFC refrigerants (R134a, R125, R32, R410A, R236ea) in a horizontal smooth tube. Int. J. Refrig., 24, 73–87.CrossRefGoogle Scholar

Cavallini, A., Censi, G., Col, Del D., Doretti, L., Longo, G. A., and Rossetto, L. (2002). Condensation of halogenated refrigerants inside smooth tubes. Heating, Ventitation, Air Conditioning and Refrigeration, 8, 429–451.Google Scholar

Cavallini, A., Censi, G., Col, Del D., Doretti, L., Longo, G. A., Rossetto, L., and Zilio, C. (2003). Condensation inside and outside smooth and enhanced tubes – A review of recent research. Int. J. Refrig., 26, 373–392.CrossRefGoogle Scholar

Cavallini, A., Col, Del D., Doretti, L., Matkovic, M., Rossetto, L., and Zilio, C. (2005). Two-phase frictional pressure gradient of R236ea, R134a and R410A inside multi-port mini-channels. Exp. Thermal-Fluid Sci., 29, 861–870.CrossRefGoogle Scholar

Cavallini, A., Doretti, L., Matkovic, M., and Rossetto, L. (2006). Update on condensation heat transfer and pressure drop inside minichannels. Heat Transfer Eng., 27, 74–87.CrossRefGoogle Scholar

Celata, G. P., Cumo, M., Farello, G. E., and Incalcaterra, P. C. (1983). Critical flows of subcooled liquid and jet forces. Presented at ASME – JSME National Heat Transf. Conf., Seattle, Washington.

Celata, G. P. (1993). Recent achievements in the thermal-hydraulics of high heat flux components in fusion reactors. Exp. Thermal. Fluid Sci., 7, 263–278.CrossRefGoogle Scholar

Celata, G. P., Cumo, M., Annibale, D' F., and Farello, G. E. (1988). The influence of noncondensible gas on two-phase critical flow. Int. J. Multiphase Flow, 14, 175–187.CrossRefGoogle Scholar

Celata, G. P., Cumo, M., and Setaro, T. (1992). Flooding in inclined pipes with obstructions. Exp. Heat Transfer, 5, 18–25.Google Scholar

Celata, G. P., Cumo, M., Farello, G. E., and Focardi, G. (1989). A comprehensive analysis of direct contact condensation of saturated steam on subcooled liquid jets. Int. J. Heat Mass Transfer, 32, 639–654.CrossRefGoogle Scholar

Celata, G. P., Cumo, M., Annibale, D' F., and Farello, G. E. (1991). Direct contact condensation of steam on droplets. Int. J. Multiphase Flow, 17, 191–211.CrossRefGoogle Scholar

Celata, G. P., Cumo, M., and Mariani, A. (1993a). Burnout in highly subcooled water flow boiling in small diameter tubes. Int. J. Heat Mass Transfer, 36, 1269–1285.CrossRefGoogle Scholar

Celata, G. P., Cumo, M., and Setaro, T. (1993b). Flooding in inclined pipes with obstructions. Exp. Therm. Fluid Sci., 5, 18–25.CrossRefGoogle Scholar

Celata, G. P., Cumo, M., Mariani, A., Nariai, H., and Inasaka, F. (1993c). Influence of channel diameter on subcooled flow boiling burnout at high heat fluxes. Int. J. Heat Mass Transfer, 36, 3407–3409.Google Scholar

Celata, G. P., Cumo, M., and Mariani, A. (1994a). Assessment of correlations and models for the prediction of Critical heat flux in water subcooled flow boiling. Int. J. Heat Mass Transfer, 37, 237–255.CrossRefGoogle Scholar

Celata, G. P., Cumo, M., Mariani, A., Simoncini, M., and Zummo, G. (1994b). Rationalization of existing mechanistic models for the prediction of water subcooled flow boiling critical heat flux. Int. J. Heat Mass Transfer, 37, Suppl. 1, 347–360.CrossRefGoogle Scholar

Celata, G. P., Mishima, K., and Zummo, G. (2001). Critical heat flux prediction for saturated flow boiling of water in vertical tubes. Int. J. Heat Mass Transfer, 44, 4323–4331.CrossRefGoogle Scholar

Chalfi, T. (2007). Pressure Loss Associated with Flow Area Changes in Microchannels. MS Thesis, Geogia Institute of Technology, Atlanta, GA.Google Scholar

Chandrasekhar, S. (1961). Hydrodynamic and Hydromagnetic Stability, Cambridge Univesrity Press, Cambridge.Google Scholar

Chang, T.-H., and Chung, J. N. (1985). The effects of surfactants on the motion and transport mechanisms of a condensing droplet in a high Reynolds number flow. AIC Homogeneous E J., 31, 1149–1156.CrossRefGoogle Scholar

Chang, J. Y., and You, S. M. (1996). Heater orientation effect on pool boiling of micro-porous-enhanced surface in saturated Forced convection-72. J. Heat Transfer, 118, 937–943.CrossRefGoogle Scholar

Chapman, S., and Cowling, T. G. (1970). The Mathematical Theory of Non-uniform Gases, 3rd ed., Cambridge University Press, Cambridge.Google Scholar

Chedester, R. C., and Ghiaasiaan, S. M. (2002). A proposed mechanism for hydrodynamically-controlled onset of significant void in microchannels. Int. J. Heat Fluid Flow, 23, 769–775.CrossRefGoogle Scholar

Chen, J. C. (1966). Correlation for boiling heat transfer to saturated fluids in convective flow. Ind. Eng. Chem. Res., 5, 322–329.Google Scholar

Chen, J. C., Ozkaynak, F. T., and Sundaram, R. K. (1979). Vapor heat transfer in post-Critical heat flux region including the effect of thermodynamic non-equilibrium. Nucl. Eng. Design, 51, 143–155.CrossRefGoogle Scholar

Chen, S. L., Gerner, F. M., and Tien, C. L. (1987). General film condensation correlations. Exp. Heat Transfer, 1, 93–107.CrossRefGoogle Scholar

Chen, W. C., Klausner, J. F., and Mei, R. (1995). A simplified model for predicting vapor bubble growth rates in heterogeneous boiling. J. Heat Transfer, 117, 976–980.CrossRefGoogle Scholar

Chen, Y., and Cheng, P. (2005). Condensation of steam in silicon microchannels. Int. Comm. Heat Mass Transfer, 32, 175–183.CrossRefGoogle Scholar

Cheng, S. C., Wong, Y. L., and Groeneveld, D.C. (1988). Critical heat flux prediction for horizontal flow. Proc. Int. Symp. on Phase Change Heat Transfer, Chonqing, China, pp. 211–215.Google Scholar

Cheng, X. (2005). Experimental studies on critical heat flux in vertical tight 37-rod bundles using Freon-12. Int. J. Multiphase Flow, 31, 1198–1219.CrossRefGoogle Scholar

Chexal, B., Abdollahian, D., and Norris, D. (1984). Analytical prediction of single-phase and two-phase flow through cracks in pipes and tubes. AIC Homogeneous Eddy diffusivity (m2/s) Symp. Ser., 80(236), 19–23.Google Scholar

Chexal, B., Lelluche, G., Horowitz, J., Healzer, J., and Oh, S. (1991). The Chexal-Lelluche void fration correlation for generalized Applications. Electric Power Research Institute, Rep. NSAC-139, Palo Alto, CA.Google Scholar

Chexal, B., Merilo, M., Maulbetsch, M., Horowitz, J.Harrison, J., Westacott, J., Peterson, C., Kastner, W., and Schmidt, H. (1997). Void fraction technology for design and analysis, Electric Power Research Institute, Palo Alto, CA.Google Scholar

Chisholm, D. (1967). A theoretical basis for the Lockhart–Martinelli correlation for two-phase flow. Int. J. Heat Mass Transfer, 10, 1767–1778.CrossRefGoogle Scholar

Chisholm, D. (1972). An equation for velocity ratio in two-phase flow. NEL Rep. 535. (cited in Whalley, 1996.)

Chisholm, D. (1973). Pressure gradients due to friction during the flow of evaporating two-phase mixture in smooth tubes and channels. Int. J. Heat Mass Transfer, 16, 347–358.CrossRefGoogle Scholar

Chisholm, D. (1980). Two-phase pressure drops in bends. Int. J. Multiphase Flow, 6, 363–367.CrossRefGoogle Scholar

Chisholm, D. (1981). Modern developments in marine condensers: Noncondensable gases: An overview. In Power Condenser Heat Transfer Technology, Marto, P. J., and Nunn, R. H., Eds., Hemisphere, New York, pp. 95–142.Google Scholar

Chisholm, D. (1985). Two-phase flow in heat exchangers and pipelines. Heat Transfer Eng., 6, 48–57.CrossRefGoogle Scholar

Chisholm, D., and Laird, A. D. K. (1958). Two-phase flow in rough tubes. Trans., ASME, 80, 276–283.Google Scholar

Cho, C., Irvine, T. F. Jr., and Karni, J. (1992). Measurement of the diffusion coefficient of naphthalene into air. Int. J. Heat Mass Transfer, 35, 957–966.Google Scholar

Choi, S. B., Barron, R. F., and Warrington, R. O. (1991). Fluid flow and heat transfer in microtubes. Proc. ASME 1991 Winter Annual Meeting, DSC-Vol. 32, pp. 123–134, ASME, New York.Google Scholar

Chun, K. R., and Seban, R. A. (1971). Heat transfer to evaporating liquid films. J. Heat Transfer, 93, 391–396.CrossRefGoogle Scholar

Chung, P.Kawaji, M.-Y., M. (2004). The effect of channel diameter on adiabatic two-phase flow characteristics in microchannels. Int. J. Multiphase Flow, 30, 735–761.CrossRefGoogle Scholar

Chung, P. M.-Y., Kawaji, M., Kawahara, A., and Shibata, Y. (2004). Two-phase flow through square and circular microchannels – Effects of channel geometry. J. Fluids Eng., 126, 546–552.CrossRefGoogle Scholar

Churchill, S. W. (1977). Frictional equation spans all fluid flow regimes. Chem. Eng., 84, 91–92.Google Scholar

Churchill, S. W., and Bernstein, M. (1977). Correlating equation for forced convection from gases and liquids to a circular cylinder in crossflow. J. Heat Transfer, 99, 300–306.CrossRefGoogle Scholar

Cicchitti, A., Lombardi, C., Silvestri, M., Solddaini, G., and Zavalluilli, R., (1960). Two-phase cooling experiments – Pressure drop, heat transfer and burnout measurement. Energia Nucleare, 7, 407–425.Google Scholar

Clift, R., Grace, J. R., and Weber, M. E. (1978). Bubbles, Drops and Particles, Academic Press, New York.Google Scholar

Coddington, P., and Macian, R. (2002). A study of the performance of void fraction correlations used in the context of drift-flux two-phase flow models. Nucl. Eng. Design, 215, 199–216.CrossRefGoogle Scholar

Cole, R., and Shulman, H. L. (1966). Bubble departure diameters at subatmospheric pressures. Chem. Eng. Symp. Ser. 62(64) 6–16.Google Scholar

Colebrook, C. R. (1939). Turbulent flow in pipes with particular reference to the transition region between the smooth and rough pipe laws. J. Inst. Civil Eng., 11, 133–156.CrossRefGoogle Scholar

Coleman, J. W., and Garimella, S. (1999). Characteristics of two-phase flow patterns in small diameter round and rectangular tubes. Int. J. Heat Mass Transfer, 42, 2869–2881.CrossRefGoogle Scholar

Coleman, J. W., and Garimella, S. (2003). Two-phase flow regimes in round, square and rectangular tubes during condensation of refrigerant R134a. Int. J. Refrig., 26, 117–128.CrossRefGoogle Scholar

Collier, J. G. (1981). Forced convection boiling. In Two-Phase Flow and Heat Transfer in Power and Process Industries, Bergles, A. E., Collier, J. G., Delhaye, J. M., Hewitt, G. F., and Mayinger, F., Eds., Hemisphere, Washington, Direct-contact.Google Scholar

Collier, J. G., and Thome, J. R. (1994). Convective Boiling and Condensation, 3rd ed., Clarendon Press, Oxford, England.Google Scholar

Collier, R. P., and Norris, D. M. (1983) Two-phase flow experiments through intergranular stress corrosion cracks. Proc., CSNI Specialist Meeting on Leak-Before Break in Nuclear Reactor Piping, U.S. Nuclear Regulatory Commission Rep. NUREG/CP-005, pp. 273–299.Google Scholar

Collier, R. P., Stuben, F. B., Mayfield, M. E., Pope, D. B., and Scott, P. M. (1984) Two-phase flow through intergranular stress corrosion cracks. Electric Power Research Institute Rep. EPRI-NP-3540-LD, Palo Alto, CA.Google Scholar

Comish, R. J. (1928). Flow in a pipe of rectangular cross-sections. Proc. R. Soc. Ser. A, 120 (A786), 691–695.Google Scholar

Cooper, M. G. (1984). Saturated nucleate pool boiling – A simple correlation. First UK National Heat Transfer Conf., Inst. Chem. Eng. Symp. Ser. 86, 2, 785–793.CrossRefGoogle Scholar

Cooper, M. G., and Lloyd, A. J. P. (1969). The microlayer in nucleate pool boiling, Int. J. Heat Mass Transfer, 12, 895–913.CrossRefGoogle Scholar

Cooper, M. G., Judd, A. M., and Pike, R. A. (1978). Shape and departure of single bubbles growing at a wall. Proc. 6th Int. Heat Transfer Conf., Toronto, 1, 115–120.Google Scholar

Cornish, R. J. (1928). Flow in a pipe of rectangular cross-section. Proc. R. Soc. Ser. A, 120, 691–700.CrossRefGoogle Scholar

Cornwell, K., and Kew, P. A. (1992). Boiling in small parallel channels. Proc. CEC Conference on Energy Efficiency in Process Technology, Athens, October, Paper 22, Elsevier Applied Science, pp. 624–638.Google Scholar

Coulaloglu, C. A., and Tavralides, L. L. (1977). Description of interaction processes in agitated liquid-liquid dispersions. Chem. Eng. Sci., 32, 1289–1297.CrossRefGoogle Scholar

Courtaud, M., Deruaz, R., and Aillon, D' L. G. (1988). The French thermal-hydraulic program addressing the requirements of the future pressurized water reactors. Nucl. Technol., 80, 73–82.CrossRefGoogle Scholar

Cumo, M., et al. (1980). Experimental advanced on boiler heat transfer. Proc., Int. Conf. Boiler Dynamics and Control in Nuclear Power Stations, 2nd, British Nuclear Society, p. 367.Google Scholar

Cussler, E. C. (1997). Diffusion Mass Transfer in Fluid Systems, 2nd ed., Cambridge University Press, Cambridge.Google Scholar

Dagan, R., Elias, E., Wacholder, E., and Olek, S. (1993). A two-fluid model for critical flashing flows in pipes. Int. J. Multiphase Flow, 19, 15–25.CrossRefGoogle Scholar

Dagan, Z. (1984). Spreading of films of adsorption on a liquid surface. PCH PhysicoChem. Hydrodyn., 5, 43–51.Google Scholar

Daleas, R. S., and Bergles, A. E. (1965). Effects of upstream compressibility on subcooled critical heat flux. Paper 65 – HT – 67, ASME, New York.Google Scholar

Daiguji, H., Hihara, E., and Saito, T. (1977). Mechanism of absorption enhancement by surfactants. Int. J. Heat Mass Transfer, 40, 1743–1752.CrossRefGoogle Scholar

Donne, Dalle M., and Hame, W. (1985). Critical heat flux for triangular arrays of rod bundles with tight lattices, including the spiral spacer effects. Nucl. Technol., 71, 111– 124.CrossRefGoogle Scholar

Damianides, C. A., and Westwater, J. W. (1988). Two-phase flow patterns in a compact heat exchanger and in small tubes. Proc. UK National Heat Transfer Cont., 2nd, pp. 1257– 1268.Google Scholar

Das, P. Y., Kumar, R., and Ramkrishna, D. (1987). Coalescence of drops in stirred dispersions, a white noise model for coalescence. Chem. Eng. Sci., 42, 213–220.CrossRefGoogle Scholar

Davidson, J. F., and Harrison, D. (1971). Fluidization, Academic Press, New York.Google Scholar

Davies, J. T., and Rideal, E. K. (1963). Interfacial Phenomena, Academic Press, New York.Google Scholar

Davis, E. J., and Anderson, G. H. (1966). The incipience of nucleate boiling in forced convection flow. AIC Homogeneous E J., 12, 774–780.CrossRefGoogle Scholar

Davis, R. M., and Taylor, G. I. (1950). The mechanism of large bubbles rising through extended liquids and through liquids in tubes. Proc. R. Soc. Ser. A, 200, 375–390.CrossRefGoogle Scholar

Ded, J. S., and Lienhard, J. H. (1972). The peak pool boiling from a sphere. AIC Homogeneous E J., 18, 337–342.CrossRefGoogle Scholar

Deissler, R. G. (1954). Analysis of turbulent heat transfer, mass transfer and friction in smooth tubes at high Prandtl and Schmidt numbers. NACA Tech Rep. 1210.Google Scholar

Delhaye, J. M. (1969). General equations for two-phase systems and their applications to air-water bubble flow and to steam-water flashing flow. ASME-69-HT-63Google Scholar

Delhaye, J. M., and Bricard, P. (1994). Interfacial area in bubbly flow: Experimental data and correlations. Nucl. Eng. Design, 151, 65–77.CrossRefGoogle Scholar

Dengler, C. E., and Addoms, J. N. (1956). Heat transfer mechanism for vaporization of water in a vertical tube. Chem. Eng. Prog. Symp. Ser., 52 (18), 85–103.Google Scholar

Salve, M., Panella, B., and Scorta, G. (1986). Heat and mass transfer by direct condensation of steam on a subcooled turbulent water jet. Proc. 8th Int. Heat Transfer Conf., San Francisco, 4, 1653–1658.Google Scholar

Dey, D., Boulton-Stone, J. M., Emery, A. N., and Blake, J. R. (1997). Experimental comparisons with a numerical model of surfactant effects on the burst of a single bubble. Chem. Eng. Sci., 52, 2769–2783.CrossRefGoogle Scholar

Young, T. L. (1975). Homogeneous equilibrium critical flow model. Aerojet Nuclear Company Internal Rep. TLD-1-75.Google Scholar

Dhir, V. K. (1991). Nucleate and transition boiling heat transfer under pool and external flow conditions. Int. J. Heat Fluid Flow, 12, 290–314.CrossRefGoogle Scholar

Dhir, V. K. (1994). Boiling and two-phase flow in porous media. Annu. Rev. Heat Transfer, 5, 303–350.CrossRefGoogle Scholar

Dhir, V. K. (1998). Boiling heat transfer. Annu. Rev. Fluid Mech., 30, 265–401.CrossRefGoogle Scholar

Dhir, V. K., and Liaw, S. P. (1989). Framework for a unified model for nucleate and transition pool boiling. J. Heat Transfer, 111, 739–746.CrossRefGoogle Scholar

Dhir, V. K., and Lienhard, J. H. (1974). Peak pool boiling heat flux in viscous liquids. J. Heat Transfer, 96, 71–78.CrossRefGoogle Scholar

Dhir, V. K., Castle, J. N., and Catton, I. (1977). Role of Taylor instability on sublimation of a horizontal slab of dry ice. J. Heat Transfer, 99, 411–418.CrossRefGoogle Scholar

Dittus, F. W., and Boelter, L. M. K. (1930). Heat transfer in automobile radiators of the tubular type. University of California Publication on Engineering, Vol. 2, No. 13, Berkeley, California.Google Scholar

Dix, G. E. (1971). Vapor void fractions for forced convection with subcooled boiling at low flow rates. Ph.D. thesis, University of California, Berkeley. Also, General Electric Rep. NEDO-10491.Google Scholar

Dobran, F. (1987). Nonequilibrium modeling of two-phase critical flow in tubes. J. Heat Transfer, 109, 731–738.CrossRefGoogle Scholar

Dobson, M. K., and Chato, J. C. (1998). Condensation in smooth horizontal tubes. J. Heat Transfer, 120, 193–213.CrossRefGoogle Scholar

Dobson, M. K., Chato, J. C., Hinde, D. K., and Wang, S. P. (1994). Experimental evaluation of internal condensation of refrigerants R-12 and R-134a, ASHRAE Trans., 100, 744–754.Google Scholar

Doroschuk, V. E., Levitan, L. L., and Lantzman, F. P. (1975). Investigation into burnout in uniformly heated tubes. ASME Paper 75-WA/HT-22.Google Scholar

Dougall, R. L., and Rohsenow, W. M. (1963). Film boiling on the inside of vertical tubes with upward flow of the fluid at low qualities. Rep. MIT-TR-9070–26, Massachusetts Institute of Technology, Cambridge, MA.Google Scholar

Downar-Zapolski, Z., Bilicki, Z., Bolle, L., and Franco, J. (1996). The non-equilibrium relaxation model for one-dimensional flashing liquid flow. Int. J. Multiphase Flow, 22, 473–483.CrossRefGoogle Scholar

Drew, D. A., and Lahey, R. T. (1987). The virtual mass and lift force on a sphere in rotating and straining inviscid flow. Int. J. Multiphase Flow, 13, 113–121.CrossRefGoogle Scholar

Drew, D. A., Cheng, L. Y., and Lahey, R. T. (1979). The analysis of virtual mass effect in two-phase flow. Int. J. Multiphase Flow, 5, 233–242.CrossRefGoogle Scholar

Dukler, A. E., and Hubbard, M. G. (1975). A model for gas-liquid slug flow in horizontal and near-horizontal tubes. Ind. Eng. Chem. Fundam., 14, 337–347.CrossRefGoogle Scholar

Dukler, A. E., and Smith, L. (1979). Two-phase interactions in countercurrent flow: Studies of the flooding mechanism. NUREG/CR-0617, U.S. Nuclear Regulatory Commission, Washington, Direct-contact.Google Scholar

Dukler, A. E., and Taitel, Y. (1986). Flow pattern transitions in gas-liquid systems: Measurement and modeling. In Multiphase Science and Technology, Hewitt, , , G. F., Delhaye, , , J. M., and Zuber, N., Eds., 2, 1–94.CrossRefGoogle Scholar

Dukler, A. E., Wicks, M., III , and Cleveland, R. G. (1964). Pressure drop and hold-up in two-phase flow. AIC Homogeneous E J., 10, 38–51.CrossRefGoogle Scholar

Dumitrescu, D. T. (1943). Strömung an einer Luftblase in senkrechten Rohr. Z. Agnew Math. Mech., 23, 139–149.CrossRefGoogle Scholar

Duncan, A. B., and Peterson, G. P. (1994). Review of microscale heat transfer. Appl. Mech. Rev., 47, 397–428.CrossRefGoogle Scholar

Eames, I. W., Marr, N. J., and Sabir, H. (1997). The evaporation of water: A review. Int. J. Heat Mass Transfer, 40, 2963–2973.CrossRefGoogle Scholar

Edvinsson, R., and Irandoust, S. (1996). Finite-element analysis of Taylor flow. AIC Homogeneous E J., 42, 1815–1823.CrossRefGoogle Scholar

Edwards, D. K., Denny, V. E., and Mills, A. F. (1979). Transfer Processes, 2nd ed., Hemisphere, Washington, Direct-contact.Google Scholar

Eichhorn, R. (1980). Dimensionless correlation of the hanging film phenomenon. J. Fluids Eng., 102, 372–375.CrossRefGoogle Scholar

Ekberg, N. P., Ghiaasiaan, S. M., Abdel-Khalik, S. I., Yoda, M., and Jeter, S. M. (1999). Gas-liquid two-phase flow in narrow horizontal annuli. Nuel. Eng. Design, 192, 59–80.CrossRefGoogle Scholar

El-Genk, M. S., and Rao, D. V. (1991a). Critical heat flux in rod bundles at low flow and low pressure conditions. ASME Heat Transfer Division, 150, Thermal Hydraulics of Advanced Nuclear Reactors, pp. 25–30.Google Scholar

El-Genk, M. S., and Rao, D. V. (1991b). On the predictions of critical heat flux in rod bundles at low flow and low pressure conditions. Heat Transfer Eng., 12, 48–57.CrossRefGoogle Scholar

El-Genk, M. S., Haynes, S. J., and Kim, S. H. (1988). Critical heat flow of water in vertical annuli. Int. J. Heat Mass Transfer, 31, 2291–2303.CrossRefGoogle Scholar

Hajal, El J., Thome, J. R., and Cavallini, A. (2003). Condensation in horizontal tubes. Part I: Two-phase flow pattern map. Int. J. Heat Mass Transfer, 46, 3349–3363.CrossRefGoogle Scholar

Elias, E., and Chambre, P. L. (1984). A mechanistic nonequilibrium model for two-phase critical flow. Int. J. Multiphase Flow, 10, 21–40.CrossRefGoogle Scholar

Elias, E., and Lelluche, G. S. (1994). Two-phase critical flow. Int. J. Multiphase Flow, 20, Suppl., 91–168.CrossRefGoogle Scholar

Elkassabgi, Y., and Lienhard, J. H. (1988). The peak pool boiling heat fluxes from horizontal cylinders in subcooled liquids. J. Heat Transfer, 110, 479–492.CrossRefGoogle Scholar

Emiliani, E. (1992). Planet Earth, Cambridge University Press, Cambridge.Google Scholar

Emmert, R. E., and Pigford, R. L. (1954). A study of gas absorption in falling liquid films. Chem. Eng. Prog., 50, 87–93.Google Scholar

Epstein, M., and Hauser, G. M. (1991). Simultaneous fog formation and thermophoretic droplet deposition in a turbulent pipe flow. J. Heat Transfer, 113, 224–231.CrossRefGoogle Scholar

Faghri, A., and Zhang, Y. (2006). Transport Phenomena in Multiphase Systems, Elsevier/Academic Press, Amsterdam.Google Scholar

Fairbrother, F., and Stubbs, A. E. (1935). Studies in electroendosmosis. Part VI. The bubble-tube method of measurements. J. Chem. Soc., 1, 527–529.CrossRefGoogle Scholar

Feburie, V., Giot, M.Granger, S., and Seynhaever, J. M. (1993). A model for choked flow through cracks with inlet subcooling. Int. J. Multiphase Flow, 19, 541–562.CrossRefGoogle Scholar

Fiori, M. P., and Bergles, A. E. (1970). Model of Critical heat flux in subcooled boiling. Proc. 4th Int. Heat Transfer Conf., Paris–Versailles, 6, Paper b6.3, Elsevier, Dordrecht.Google Scholar

Fisher, S. A., Harrison, G. S., and Pearce, D. C. (1978). Premature dryout in conventional and nuclear power station evaporators. Proc. 6th Int. Heat Transfer Conf., Toronto, 2, 49– 54.Google Scholar

Fletcher, D. F. (1991). An improved mathematical model of melt/water detonation – I. Model formulation and example results. Int. J. Heat Mass Transfer, 34, 2435–2448.CrossRefGoogle Scholar

Fluent Inc. (2005). Fluent 6.2.16 User's Guide.

Fluid Dynamics International, Inc., Evanston, IL 60210 (1991).

Foda, M., and Cox, R. G. (1980). The spreading of thin liquid films on a water-air interface. J. Fluid Mech., 101, 33–51.CrossRefGoogle Scholar

Ford, J. D., and Lekic, A. (1973). Rate of growth of drops during condensation. Int. J. Heat Mass Transfer, 16, 61–64.CrossRefGoogle Scholar

Forster, H. K., and Greif, R. (1959). Heat transfer to boiling liquid, mechanism and correlations. J. Heat Transfer, 81, 43–53.Google Scholar

Forster, H. K., and Zuber, N. (1954). Growth of a vapor bubble in a superheated liquid. J. Appl. Phys., 25, 474–478.CrossRefGoogle Scholar

Forster, H. K., and Zuber, N. (1955). Dynamics of vapor bubbles and boiling heat transfer. Chem. Eng. Prog., 1(4), 531–535.Google Scholar

Fourar, M., and Bories, S. (1995). Experimental study of air-water two-phase flow through a fracture (narrow channel). Int. J. Multiphase Flow, 21, 621–637.CrossRefGoogle Scholar

Friedel, L. (1979). Improved pressure drop correlations for horizontal and vertical two-phase pipe flow. 3R Int., 18, 485–492.Google Scholar

Friedlander, S. K. (2000). Smoke, Dust, and Haze, 2nd ed., Oxford University Press, London.Google Scholar

Fritz, W. (1935). Maximum volume of vapor bubbles. Phys. Z., 36, 379–384.Google Scholar

Fu, B. R., and Pan, C. (2005). Flow pattern transition instability in a microchannel with CO2 bubbles produced by chemical reactions. Int. J. Heat Mass Transfer, 48, 4397–4409.CrossRefGoogle Scholar

Fujii, T., Uehara, H., Hirata, K., and Oda, K. (1972). Heat transfer and flow resistance in condensation of low pressure steam flowing through tube banks. Int. J. Heat Mass Transfer, 15, 247–260.CrossRefGoogle Scholar

Fujita, T., and Ueda, T. (1978). Heat transfer to falling liquid films and film breakdown – I Subcooled liquid films. Int. J. Heat Mass Transfer, 21, 97–108.CrossRefGoogle Scholar

Fukano, T., and Kariyasaki, A. (1993). Characteristics of gas-liquid two-phase flow in a capillary. Nucl. Eng. Design, 141, 59–68.CrossRefGoogle Scholar

Fukano, T., Kariyasaki, A., and Kagawa, M. (1989). Flow patterns and pressure drop in isothermal gas-liquid concurrent flow in a horizontal capillary tube. Proc., 1989 National Heat Transfer Conf., Tilmaz, S. B., Ed., American Nuclear Society, pp. 153–161.Google Scholar

Fulford, G. D. (1964). The flow of liquids in thin films. Adv. Chem. Eng., 5, 151–236.CrossRefGoogle Scholar

Gadis, E. S. (1972). The effect of liquid motion induced by phase change and thermocapillary on the thermal equilibrium of a vapor bubble. Int. J. Heat Mass Transfer, 15, 2241–2250.Google Scholar

Gaertner, R. F. (1965). Photographic study of nucleate pool boiling on a horizontal surface. J. Heat Transfer, 87, 17–29.CrossRefGoogle Scholar

Galloway, J. E., and Mudawar, I. (1993). Critical heat flux mechanism in flow boiling from a short heated wall – I. Examination of near-wall conditions with the aid of photomicrography and high-speed video imaging. Int. J. Heat Mass Transfer, 36, 2511–2526.CrossRefGoogle Scholar

Ganchev, B., Zozlov, V., and Lozovetskiy, V. (1972). A study of heat transfer to a falling liquid film at a vertical surface. Heat Transfer Sov. Res., 4 (2), 102–110.Google Scholar

Ganic, E. N., and Mastanaiah, K. (1983). Hydrodynamics and heat transfer in falling film flow. In Low Reynolds Number Flow Heat Exchangers, Kakac, S., Shah, R., and Bergles, A. E., Eds., Hemisphere, Washington, Direct-contact.Google Scholar

Garimella, S., and Bandhauer, T. M. (2001). Measurement of condensation heat transfer coefficients in microchannel tubes. Proc. 2001 IMECE, ASME, New York.Google Scholar

Garimella, S., Killion, J. D., and Coleman, J. W. (2002). An experimentally validated model for two-phase pressure drop in the intermittent flow regime for circular microchannels. J. Fluids Eng., 124, 205–214.CrossRefGoogle Scholar

Garrels, R. M., and Christ, C. L. (1965). Solutions, Minerals and Equilibria, Harper and Rowe, New York.Google Scholar

Geiger, G. E., and Rohrer, W. M. (1966). Sudden contraction losses in two-phase flow. J. Heat Transfer, 88, 1–9.CrossRefGoogle Scholar

Geng, H., and Ghiaasiaan, S. M. (1998). Mechanistic modeling of critical flow of initially subcooled liquid containing dissolved noncondensables through cracks and slits based on the homogeneous-equilibrium mixture method. Nucl. Sci. Eng., 129, 294–304.CrossRefGoogle Scholar

Geng, H., and Ghiaasiaan, H. (2000). Mechanistic nonequilibrium modeling of critical flow of subcooled liquids containing dissolved noncondensables using the dynamic flow regime model. Proc. 8th Int. Conf. on Nuclear Engineering (ICONE-8), Paper No. ICONE-8708, Baltimore, MD.Google Scholar

Ghiaasiaan, S. M. and Abdel-Khalik, S. I. (2001). Two-Phase Flow in Microchannels, Advances in Heat Transfer, Hartnett, J. P. and Irvine, T. F. Jr., Eds., Vol. 34, pp. 145–254, Academic Press.Google Scholar

Ghiaasiaan, S. M., and Catton, I. (1983). Multi-dimensional and two-phase flow effects in Pressurized water reactor core reflooding. Electric Power Research Institute Rep. EPRI NP-3437, Palo Alto, CA.Google Scholar

Ghiaasiaan, S. M., and Chedester, R. C. (2002). Boiling incipience in microchannels. Int. J. Heat Mass Transfer, 45, 4599–4606.CrossRefGoogle Scholar

Ghiaasiaan, S. M., and Eghbali, D. A. (1997). On modeling of turbulent vapor condensation with noncondensables. J. Heat Transfer, 119, 373–376.CrossRefGoogle Scholar

Ghiaasiaan, S. M., and Geng, H. (1997). Mechanistic non-equilibrium modeling of critical flashing flow of subcooled liquids containing dissolved noncondensables. Num. Heat Transfer B, 32, 435–457.CrossRefGoogle Scholar

Ghiaasiaan, S. M., and Laker, T. S. (2001). Turbulent forced convection in microtubes. Int. J. Heat Mass Transfer, 44, 2777–2782.CrossRefGoogle Scholar

Ghiaasiaan, S. M., Catton, I., and Duffey, R. B. (1985). Thermal-hydraulics and two-phase phenomena during reflooding of nuclear reactor cores. J. Fluids Eng., 85, 89–96.Google Scholar

Ghiaasiaan, S. M., Wassel, A. T., and Lin, C. S. (1991). Direct contact condensation in the presence of noncondensables in OC-OTEC condensers, J. Solar Energy Eng., 113, 228–235.CrossRefGoogle Scholar

Ghiaasiaan, S. M., Kamboj, B. K., and Abdel-Khalik, S. I. (1995). Two-fluid modeling of condensation in the presence of noncondensables in two-phase channel flow. Nucl. Sci. Eng., 119, 1–17.CrossRefGoogle Scholar

Ghiaasiaan, S. M., Wu, X., Sadaowski, D. L., and Abdel-Khalik, S. I. (1997a). Hydrodynamic characteristics of counter-current two-phase flow in vertical and inclined channels: Effects of liquid properties. Int. J. Multiphase Flow, 23, 1063–1083.CrossRefGoogle Scholar

Ghiaasiaan, S. M., Muller, J. R., Sadowski, D. L., and Abdel-Khalik, S. I. (1997b). Critical flow of initially highly subcooled water through a short capillary. Nucl. Sci. Eng., 126, 229– 238.CrossRefGoogle Scholar

Giavedoni, M. D., and Saita, F. A. (1997). The axisymmetric and plane cases of a gas phase steadily displacing a Newtonian liquid – A simultaneous solution of the governing equations. Phys. Fluids, 9, 2420–2428.CrossRefGoogle Scholar

Giavedoni, M. D., and Saita, F. A. (1999). The rear meniscus of a long bubble steadily displacing a Newtonian liquid in a capillary tube. Phys. Fluids, 11, 786–794.CrossRefGoogle Scholar

Giot, M., and Fritz, A. (1972). Two-phase two- and one-component critical flow with the variable slip model. Prog. Heat Transfer, 6, 651–670.Google Scholar

Gnielinski, V. (1976). New equations for heat and mass transfer in Turbulent pipe and channel flow. Int. Chem. Eng. 16, 359–368.Google Scholar

Golden, S. (1964) Elements of the Theory of Gases, Addison-Wesley, Reading, MA.Google Scholar

Gombosi, T. I. (1994). Gaskinetic Theory, Cambridge University Press, Cambridge.CrossRefGoogle Scholar

Gorenflo, D. (1993). Pool boiling. In VDI-Heat Atlas (English Version), Schlünder, E. U., Ed., pp. Ha 1–13, VDI-Verlag, Düsseldorf, Germany.Google Scholar

Gorenflo, D., Chandra, U., Kotthoff, S., and Luke, A. (2004). Influence of thermophysical properties on pool boiling heat transfer of refrig. Int. J. Refrige., 27, 392–502.CrossRefGoogle Scholar

Gorenflo, D., Knabe, V., and Bieling, V. (1986). Bubble density on surfaces with nucleate boiling – Its influence on heat transfer and burnout heat flux at elevated saturation pressures. Proc. 8th Int. Heat Transfer Conf., San Francisco, 4, 1995–2000.Google Scholar

Govier, F. W., and Aziz, K. (1972). The Flow of Complex Mixtures in Pipes, Robert E. Krieger, Malabar, FL.Google Scholar

Griffith, P., and Wallis, J. D. (1960). The role of surface conditions in nucleate boiling. Chem. Eng. Symp. Ser. 56, 30, 49–63.Google Scholar

Griffith, P., Clark, J. A., and Rohsenow, W. W. (1958). Void volumes in subcooled boiling systems. ASME Paper 58-HT-19.

Grober, H., Erk, S., and Grigull, U. (1961). Fundamentals of Heat Transfer, McGraw-Hill, New York.Google Scholar

Groeneveld, D. C. (1973). Post-dryout heat transfer at reactor operating conditions. American Nuclear Society Topical Meeting on Water Reactor Safety, Salt Lake City.Google Scholar

Groeneveld, D. C., and Delorme, G. G. J. (1976). Prediction of thermal non-equilibrium in the post-dryout regime. Nucl. Eng. Design, 36, 17–26.CrossRefGoogle Scholar

Groeneveld, D. C., and Snoek, C. W. (1986). A comprehensive examination of heat transfer correlations suitable for reactor safety analysis. In Multiphase Science and Technology, Hewitt, , , G. F., Delhaye, J. M., and Zuber, , , N., Eds., Hemisphere, Washington, Direct-contact, 2, 181–274.CrossRefGoogle Scholar

Groeneveld, D. C., Cheng, S. C., and Doan, T. (1986). AECL-UO critical heat flux look-up table. Heat Transfer Eng., 7, 46–62.CrossRefGoogle Scholar

Groeneveld, D. C., Leung, L. K. H., Kirillov, P. I., Bobkov, V. P., Smogalev, I. P., Vinogradov, V. N., Huang, X. C., and Royer, E. (1996). The 1995 look-up table for critical heat flux in tubes, Nucl. Eng. Design, 163, 1–23.CrossRefGoogle Scholar

Groeneveld, D. C., Leung, L. K. H., Vasic, A. Z., Guo, Y. J., and Cheng, S. C. (2003). A look-up table for fully-developed film boiling heat transfer. Nucl. Eng. Design, 225, 83–97.CrossRefGoogle Scholar

Grohmann, S. (2005). Measurement and modeling of single-phase and flow boiling heat transfer in microtubes. Int. J. Heat Mass Transfer, 48, 4073–4089.CrossRefGoogle Scholar

Guglielmini, G., Lorenzi, A., Muzzio, A., and Sotgia, G. (1986). Two-phase flow pressure drops across sudden area contractions. Proc. 8th Int. Heat Transfer Conf., Vol. 5, pp. 2361–2366, ASME, New York.Google Scholar

Gungor, K. E., and Winterton, R. H. S., 1986. A general correlation for flow boiling in tubes and annuli, Int. J. Heat Mass Transfer, 29, 351–358.CrossRefGoogle Scholar

Gungor, K. E., and Winterton, R. H. S (1987). Simplified general correlation for saturated flow boiling and Comparison of correlations with data. Chem. Eng. Res. Des., 65, 148–156.Google Scholar

Habib, I. S., and Na, T. Y. (1974). Prediction of heat transfer in turbulent pipe flow with constant wall temperature. J. Heat Transfer, 96, 253–254.CrossRefGoogle Scholar

Hadamard, J. (1911). Movement permenant lent d'une sphere liquide et visqueuse dans une liquide visqueux. J. Comp. Rend, 152, 1735.Google Scholar

Hainoun, A., Hicken, E., and Wolters, J. (1996). Modeling of void formation in the subcooled boiling regime in the ATHLET code to simulate flow instability for research reactors. Nucl. Eng. Design, 167, 175–191.CrossRefGoogle Scholar

Hall, D. D., and Mudawar, I. (1997). Evaluation of subcooled Critical heat flux correlations using the PU-BTPFL Critical heat flux database for vertical upflow of water in a uniformly heated round tube. Nucl. Technol., 117, 234–246.CrossRefGoogle Scholar

Hall, D. D., and Mudawar, I. (2000a). Critical heat flux (Critical heat flux) for water flow in tubes – I. Compilation and assessment of world Critical heat flux data. Int. J. Heat Mass Transfer, 43, 2573–2604.CrossRefGoogle Scholar

Hall, D. D., and Mudawar, I. (2000b). Critical heat flux (Critical heat flux) for water flow in tubes – II. Subcooled Critical heat flux correlations. Int. J. Heat Mass Transfer, 43, 2605–2640.CrossRefGoogle Scholar

Hampton, H. (1951). The condensation of steam on a metal surface. Proc. General Discussion of Heat Transfer, Inst. Mech. Eng. and ASME, 84, 58–64.Google Scholar

Han, C. Y., and Griffith, P. (1965). The mechanism of heat transfer in nucleate pool boiling, Part I. Bubble initiation, growth and departure. Int. J. Heat Mass Transfer, 8, 887–904.Google Scholar

Hanratty, T. J., and Hershman, A. (1961). Initiation of roll waves. AIC Homogeneous E J., 7, 488–497.CrossRefGoogle Scholar

Hapke, J., Boye, H., and Schmidt, J. (2000). Onset of nucleate boiling in microchannels. Int. J. Thermal Sci., 39, 505–513.CrossRefGoogle Scholar

Haramura, Y. (1999). Critical heat flux in pool boiling. In Handbook of Phase Change, Kandlikar, S. G., Shoji, M., and Dhir, V. K., Eds, Taylor and Francis, London, Chapter 6.Google Scholar

Haramura, Y., and Katto, Y. (1983). A new hydrodynamic model of critical heat flux, applicable widely to both pool and forced convection boiling on submerged bodies in saturated liquids. Int. J. Heat Mass Transfer, 26, 389–399.CrossRefGoogle Scholar

Hardy, P., and Mali, P. (1983). Validation and development of a model describing subcooled critical flow through long tubes. Energie Primaire, 18, 5–23.Google Scholar

Hari, S., and Hassan, Y. A. (2002). Improvement of the subcooled boiling model for low pressure conditions in thermal-hydraulic codes. Nucl. Eng. Design, 216, 139–152.CrossRefGoogle Scholar

Harmathy, T. Z. (1960). Velocity of large drops and bubbles in media of infinite and restricted extent. AIC Homogeneous E.J., 6, 281–288.CrossRefGoogle Scholar

Harper, M. J., and Rich, J. C. (1993). Radiation-induced nucleation in superheated liquid droplet neutron detectors. Nucl. Instrum. Methods Phys. Res. A, 336, 220–225.CrossRefGoogle Scholar

Hasson, D., Luss, D., and Peck, R. (1964). Theoretical analysis of vapor condensation on laminar liquid jets. Int. J. Heat Mass Transfer, 7, 969–981.CrossRefGoogle Scholar

Hatton, A. P., and Hall, I. S. (1966). Photographic study of boiling on prepared surfaces. Proc. 3rd Int. Heat Transfer Conf., Chicago, 4, 24–37.Google Scholar

Haynes, B. S., and Fletcher, D. F. (2003). Subcooled flow boiling heat transfer in narrow passages. Int. J. Heat Mass Transfer, 46, 3673–3682.CrossRefGoogle Scholar

Hegab, H. E., Bari, A., and Ameel, T. (2002). Friction and convection studies of R-134a in microchannels within transition and turbulent flow regimes. Exp. Thermal Fluid Sci., 15, 245–259.Google Scholar

Heil, M. (2001). Finite Reynolds number effects in the Bretherton problem. Phys. Fluids, 13, 2517–2531.CrossRefGoogle Scholar

Heiszwolf, J. J., Engelvaart, L. B., Eijnden, Vanden M. G., Kreutzer, M. T., Kapteijn, F., and Moulijn, J. A. (2001). Hydrodynamic aspects of the monolith loop reactor. Chem. Eng. Sci., 56, 805–812.CrossRefGoogle Scholar

Henry, R. E. (1970). Two-phase critical flow at low qualities. Nucl. Sci. Eng., 41, 79–98.CrossRefGoogle Scholar

Henry, R. E. (1974). A correlation for the minimum film boiling temperature. Chem. Eng. Prog. Symp. Series, 70, 81–90.Google Scholar

Henry, R. E., and Fauske, H. K. (1971). The two-phase critical flow of one-component mixtures in nozzles, orifices, and short tubes. J. Heat Transfer, 93, 179–187.CrossRefGoogle Scholar

Henstock, W. H., and Hanratty, T. J. (1976). The interfacial drag and height of the wall layer in annular flows. AIC Homogeneous E J., 22, 990–1000.CrossRefGoogle Scholar

Herwig, H., and Hausner, O. (2003). Critical view on ‘New results in micro-fluid mechanics: An example.’ Int. J. Heat Mass Transfer, 46, 935–937.CrossRefGoogle Scholar

Hetsroni, G., Mosyak, A., Segal, Z., and Pogrebnyak, E. (2003). Two-phase flow patterns in parallel micro-channels. Int. J. Multiphase Flow, 29, 341–360.CrossRefGoogle Scholar

Heun, M. K. (1995). Performance and Optimization of microchannel condensers. Pressure (N/m2); Legendre polynomialh.D. thesis, University of Illinois, Urbana-Champagne, IL.Google Scholar

Hewitt, G. F. (1977). Mechanism and prediction of burnout. In Two-Phase Flows and Heat Transfer, Kakac, S., and Veziroglu, T. N., Eds., Hemisphere, Washington, Direct-contact, 2, 721–745.Google Scholar

Hewitt, G. F. (1983). Gas-liquid flow. In Heat Exchanger Design Handbook, Schlünder, E.U., Editor-in-chief, Hemisphere, Washington, Direct-contact, 2, 229–238.Google Scholar

Hewitt, G. F., and Govan, A. H. (1990). Phenomena and prediction in annular two-phase flow. In ASME Advances in Gas-Liquid Flows, ASME, New York, FED- 99, 41–56.Google Scholar

Hewitt, G. F., and Roberts, D. N. (1969). Studies of Two-Phase Flow Pattenrs by Simultaneous X-Ray and Flash Photography. AERE-M 2159.

Hewitt, G. F., and Wallis, G. B. (1963). Flooding and associated phenomena: Falling film flow in a vertical tube. AERE-R4022, UKAEA, Harwell, England.Google Scholar

Hibiki, T., and Ishii, M. (2001). Interfacial area concentration in steady fully-developed bubbly flow. Int. J. Heat Mass Transfer, 44, 3443–3461.CrossRefGoogle Scholar

Hibiki, T., and Ishii, M. (2002). One-dimensional drift flux model for two-phase flow in a large diameter pipe. Int. J. Heat Mass Transfer, 46, 1773–1790.CrossRefGoogle Scholar

Hibiki, T., and Ishii, M. (2003). One-dimensional drift flux model and constitutive equations for relative motion between phases in various two-phase flow regimes. Int. J. Heat Mass Transfer, 46, 4935–4948.CrossRefGoogle Scholar

Hibiki, T., and Ishii, M. (2005). Erratum to “One-dimensional drift flux model and constitutive equations for relative motion between phases in various two-phase flow regimes.” Int. J. Heat Mass Transfer, 48, 1222–1223.CrossRefGoogle Scholar

Hibiki, T., and Mishima, K. (2001). Flow regime transition criteria for upward two-phase flow in vertical narrow rectangular channels. Nucl. Eng. Design, 203, 117–131.CrossRefGoogle Scholar

Hickox, C. E. (1971). Instability due to viscosity and density stratification in axisymmetric pipe flow. Phys. Fluids, 14, 251–262.CrossRefGoogle Scholar

Hindmarsh, A. C. (1980). LSODE and LSODI, two new initial value ordinary differential equation solvers. ACM Newsl., 15 (5), 10.CrossRefGoogle Scholar

Hino, R., and Ueda, T. (1985). Studies on heat transfer and flow characteristics in subcooled flow boiling – Part I. Boiling characteristics. Int. J. Heat Mass Transfer, 11, 269–281.Google Scholar

Hinze, J. O. (1955). Fundamentals of the hydrodynamic mechanism of splitting in dispersion processes. AIC Homogeneous E J., 1, 289–295.CrossRefGoogle Scholar

Hinze, J. O. (1975). Turbulence, McGraw-Hill, New York.Google Scholar

Hirschfelder, J., Curtiss, C. F., and Bird, R.. (1954). Molecular Theory of Gases and Liquids, Wiley, New York.Google Scholar

Hopkins, N. E. (1950). Rating the restrictor tube. Refrig. Eng., 58, 1087–1095.Google Scholar

Hosaka, S., Hirata, M., and Kasagi, N. (1990). Forced convective subcooled boiling heat transfer and Critical heat flux in small diameter tubes. Proc., Int. Heat Transfer Conf., 9th, 2, 129–134.Google Scholar

Howell, J. R., and Siegel, R. (1967). Activation, growth and detachment of boiling bubbles in water from artificial nucleation sites of known geometry and size. NASA TN-0-4201.

Hsu, Y. Y. (1962). On the size range of active nucleation sites on a heating surface. J. Heat Transfer, 84C, 207–216.CrossRefGoogle Scholar

Hsu, Y. Y. (1981). Boiling heat transfer equations. In Thermohydraulics of Two-Phase Systems for Industrial Design and Nuclear Engineering, Delhaye, J. M., Giot, M., and Riethermuller, M. L., Eds., McGraw-Hill, New York, 255–296.Google Scholar

Hsu, Y. Y., and Graham, R. W. (1961). An analytical and experimental study of the thermal boundary layer and ebullition cycle in nucleate boiling. NASA TND-594.

Hsu, Y. Y., and Graham, R. W. (1986). Transport Processes in Boiling and Two-Phase Systems, American Nuclear Society, La Grange Park, IL.Google Scholar

Hsu, Y. Y., and Westwater, J. W. (1960). Approximate theory for film boiling on vertical surfaces. Chem. Eng. Prog. Symp. Ser. 56, 30, 15–24.Google Scholar

Hu, L.-W., and Pan, C. (1995). Prediction of void fraction in convective subcooled boiling channels using a one-dimensional two-fluid model. J. Heat Transfer, 117, 799–803.CrossRefGoogle Scholar

Huang, W. S., and Kintner, R. C. (1968). Effects of surfactants on mass transfer inside drops. AIC Homogeneous E J. 15, 735–744.CrossRefGoogle Scholar

Hubbard, G. L., Mills, A. F., and Chung, D. K. (1976). Heat transfer across a turbulent falling film with cocurrent vapor flow. J. Heat Transfer, 98, 319–320.CrossRefGoogle Scholar

Huber, J. B., Rewerts, L. E., and Pale, M. B. (1994a). Shell-side condensation heat transfer of R-134a – Part I: Finned-tube performance. ASHRAE Trans., 100(2), 239–247.Google Scholar

Huber, J. B., Rewerts, L. E., and Pale, M. B. (1994b). Shell-side condensation heat transfer of R-134a – Part II: Enhanced tube performance. ASHRAE Trans., 100(2), 248–256.Google Scholar

Huber, J. B., Rewerts, L. E., and Pale, M. B. (1994c). Shell-side condensation heat transfer of R-134a – Part III: Comparison with R-12. ASHRAE Trans., 100(2), 257–264.Google Scholar

Huebsch, W. W., and Pale, M. B. (2004). A comprehensive study of shell-side condensation on integral-fin tubes with R-114 and R-236ea. ASHRAE Trans., 110, Part 1, 40–52.Google Scholar

Hulburt, H. M., and Katz, S. (1964). Some problems in particle technology. A statistical mechanical formulation. Chem. Eng. Sci., 19, 555–574.CrossRefGoogle Scholar

Hwang, J. J., Tseng, F. G., and Pan, C. (2005). Ethanol–CO2 two-phase flow in diverging and converging microchannels. Int. J. Multiphase Flow, 31, 548–570.CrossRefGoogle Scholar

Idelchik, I. E. (1994). Handbook of Hydraulic Resistances, 3rd ed., CRC Press, London.Google Scholar

Inasaka, F., and Nariai, H. (1993). Critical heat flux of subcooled flow boiling with water for high heat flux application. SPIE, High Heat Flux Eng. II, 1997, 328–339.CrossRefGoogle Scholar

Inasaka, F., Nariai, H., and Shimura, T. (1989). Pressure drops in subcooled boiling in narrow tubes. Heat Transfer Jpn. Res., 18, 70–82.Google Scholar

Incropera, F. P., Dewitt, D. P., Bergman, T. L., and Lavine, A. S. (2007). Fundamentals of Heat and Mass Transfer, 6th ed., Wiley, New York.Google Scholar

International Association for the Properties of Water and Steam (1994). IAPWS release on surface tension of ordinary water substance. Available at http:/www.iapws.org/.

Isachenko, V. P., et al. (1971). Investigation of heat transfer with steam condensation on turbulent liquid jets. Teploenergetika, 18(2), 7–10.Google Scholar

Ishii, M. (1971). Thermally-induced flow instabilities in two-phase mixtures in thermal equilibrium. Pressure (N/m2); Legendre polynomialh. Tube or jet diameter (m). thesis, Georgia Institute of Technology, Atlanta, GA.

Ishii, M. (1975). Thermo-Fluid Dymainc Theory of Two-Phase Flow, Eyrolles, Paris.

Ishii, M. (1976). Study of flow instabilities in two-phase mixtures. ANL-76–23, Argonne National Laboratory, IL.CrossRef

Ishii, M. (1977). One-dimensional drift flux model and constitutive equations for relative motion between phases in various two-phase flow regimes. ANL Rep. ANL-77-47.CrossRef

Ishii, M., and Mishima, K. (1984). Two-fluid model and hydrodynamic constitutive relations. Nucl. Eng. Design, 82, 107–126.CrossRefGoogle Scholar

Ishii, M., Kim, S., and Uhle, J. (2002). Interfacial area transport equation: Model development and benchmark experiments. Int. J. Heat Mass Transfer, 45, 3111–3123.CrossRefGoogle Scholar

Ishii, M., Paranjape, S. S., Kim, S., and Sun, X. (2004). Interfacial structures and interfacial area transport in downward two-phase bubbly flow. Int. J. Heat Mass Transfer, 30, 779–801.Google Scholar

Iwamura, T., Watanabe, H., and Murao, Y. (1994). Critical heat flux experiments under steady-state and transient conditions and visualization of Critical heat flux phenomena with neutron radiography. Nucl. Eng. Design, 149, 195–206.CrossRefGoogle Scholar

Jasper, J. J. (1972). The surface tension of pure liquid compounds. J. Phys. Chem. Ref. Data, 1, 841–1010.CrossRefGoogle Scholar

Jaster, H., and Cosky, P. G. (1976). Condensation heat transfer in a mixed flow regime. Int. J. Heat Mass Transfer, 19, 95–99.CrossRefGoogle Scholar

Jayanti, S., and Hewitt, G. F. (1992). Prediction of the slug-to-churn flow transition in vertical two-phase flow. Int. J. Multiphase Flow, 18, 847–860.CrossRefGoogle Scholar

Jayawardena, S. S., Balakotaiah, V., and Witte, L. C. (1997). Flow pattern transition maps for microgravity two-phase flows. AIC Homogeneous E J., 43, 1637–1640.CrossRefGoogle Scholar

Jens, W. H., and Lottes, P. A. (1951). Analysis of heat transfer, burnout, pressure drop and density data for high pressure water. Rep. ANL-4627, US Argonne National Laboratory, Argonne, IL.

Jepsen, D. M., Azzopardi, B. J., and Whalley, P. B. (1989). The effect of gas properties on drops in annular flow. Int. J. Multiphase Flow, 15, 327–339.CrossRefGoogle Scholar

Jiang, L., Wong, M., and Zohar, Y. (1999). Phase change in microchannel heat sinks with integrated temperature sensors. J. Microelectromech. Syst., 8, 358–365.CrossRefGoogle Scholar

Jiang, L., Wong, M., and Zohar, Y. (2001). Forced convection boiling in a microchannel heat sink. J. Microelectromech. Syst., 10, 80–87.CrossRefGoogle Scholar

John, H., Reimann, J., Westphal, F., and Friedel, L. (1988). Critical two-phase flow through rough slits. Int. J. Multiphase Flow, 14, 155–174.CrossRefGoogle Scholar

Jones, O. C. Jr. (1976). An improvement in the calculation of turbulent friction in rectangular ducts, J. Fluid Eng., 98, 173–181.CrossRefGoogle Scholar

Jones, O. C., Jr., and Zuber, N. (1979). Slug-annular transition with particular reference to narrow rectangular ducts. In Two-Phase Momentum, Heat and Mass Transfer in Chemical, Process and Energy Engineering Systems, Durst, , , F., Tsiklauri, , , G. V., and Afgan, , , N., Eds., Hemisphere, Washington, Direct-contact, 1, 345–355.Google Scholar

Joos, P., and Pinters, J, (1977). Spreading kinetics of liquids on liquids. J. Colloid Interface Sci., 60, 507–513.CrossRefGoogle Scholar

Judd, R. L., and Chopra, A. (1993). Interaction of the nucleation process occurring at adjacent nucleation sites. J.Heat Transfer, 115, 955–962.CrossRefGoogle Scholar

Kagayama, T., Peterson, P. F., and Schrock, V. E. (1993). Diffusion layer modeling for condensation in vertical tubes with noncondensable gases. Nucl. Eng. Design, 141, 289–302.CrossRefGoogle Scholar

Kandlikar, S. G. (1990). A general correlation for two-phase flow boiling heat transfer coefficients inside horizontal and vertical tubes. J. Heat Transfer, 112, 219–228.CrossRefGoogle Scholar