Characterization of diabatic two-phase flows in microchannels: Flow parameter results for R-134a in a 0.5 mm channel

By Rémi Revellin, V. Dupont, T. Ursenbacher, John Richard Thome, I. Zun. 2006

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A new type of diabatic flow pattern map for boiling heat transfer in microchannels (2007, methodology): “nonexistent for mass fluxes greater than 1000 kg m −2 s −1 . Their transitions are controlled primarily by the rate of coalescence as shown in Revellin et al (2006) , which is not recognized as a contributing factor by previous microscale (nor macroscale) flow pattern maps.”
Effects of channel dimension, heat flux, and mass flux on flow boiling regimes in microchannels (2009, background): “8 1 0 500 1000 1500 w = 100 m w = 250 m w = 400 m w = 1000 m w = 2200 m w = 5850 m Revellin et al. (2006) Coleman & Garimella (2003)”
Review and Comparative Analysis of Studies on Saturated Flow Boiling in Small Channels (2008, unknown): “(2006) [111] R-134a in glass circular Dh = 0.”
Current methods for characterising mixing and flow in microchannels (2010, methodology): “Another optical method to characterise bubbles and gas–liquid flow regimes has been described by Revellin et al. (2006, 2008).”
A comprehensive flow regime map for microchannel flow boiling with quantitative transition criteria (2010, methodology): “In recent yea rs, few studies [7-11] have developed flow regime maps for boiling in microchannels using similar axe s as conventional maps with flow regime definitions pertinent to microscale boiling, and have shown tha t flow regime maps developed for larger tubes are”