%0 Journal Article %1 Thome2004128 %A Thome, John R. %D 2004 %J International Journal of Heat and Fluid Flow %K 2004 boiling experiment micro-channel review theory %N 2 %P 128 - 139 %R 10.1016/j.ijheatfluidflow.2003.11.005 %T Boiling in microchannels: a review of experiment and theory %U http://dx.doi.org/10.1016/j.ijheatfluidflow.2003.11.005 %V 25 %X A summary of recent research on boiling in microchannels is presented. The review addresses the topics of macroscale versus microscale heat transfer, two-phase flow regimes, flow boiling heat transfer results for microchannels, heat transfer mechanisms in microchannels and flow boiling models for microchannels. In microchannels, the most dominant flow regime appears to be the elongated bubble mode that can persist up to vapor qualities as high as 60–70% in microchannels, followed by annular flow. Flow boiling heat transfer coefficients have been shown experimentally to be dependent on heat flux and saturation pressure while only slightly dependent on mass velocity and vapor quality. Hence, these studies have concluded that nucleate boiling controls evaporation in microchannels. Instead, a recent analytical study has shown that transient evaporation of the thin liquid films surrounding elongated bubbles is the dominant heat transfer mechanism as opposed to nucleate boiling and is able to predict these trends in the experimental data. Newer experimental studies have further shown that there is in fact a significant effect of mass velocity and vapor quality on heat transfer when covering a broader range of conditions, including a sharp peak at low vapor qualities at high heat fluxes. Furthermore, it is concluded that macroscale models are not realistic for predicting flowing boiling coefficients in microchannels as the controlling mechanism is not nucleate boiling nor turbulent convection but is transient thin film evaporation (also, microchannel flows are typically laminar and not turbulent as assumed by macroscopic models). A more advanced three-zone flow boiling model for evaporation of elongated bubbles in microchannels is currently under development that so far qualitatively describes all these trends. Numerous fundamental aspects of two-phase flow and evaporation remain to be better understood and some of these aspects are also discussed.

@article{Thome2004128, abstract = {A summary of recent research on boiling in microchannels is presented. The review addresses the topics of macroscale versus microscale heat transfer, two-phase flow regimes, flow boiling heat transfer results for microchannels, heat transfer mechanisms in microchannels and flow boiling models for microchannels. In microchannels, the most dominant flow regime appears to be the elongated bubble mode that can persist up to vapor qualities as high as 60–70% in microchannels, followed by annular flow. Flow boiling heat transfer coefficients have been shown experimentally to be dependent on heat flux and saturation pressure while only slightly dependent on mass velocity and vapor quality. Hence, these studies have concluded that nucleate boiling controls evaporation in microchannels. Instead, a recent analytical study has shown that transient evaporation of the thin liquid films surrounding elongated bubbles is the dominant heat transfer mechanism as opposed to nucleate boiling and is able to predict these trends in the experimental data. Newer experimental studies have further shown that there is in fact a significant effect of mass velocity and vapor quality on heat transfer when covering a broader range of conditions, including a sharp peak at low vapor qualities at high heat fluxes. Furthermore, it is concluded that macroscale models are not realistic for predicting flowing boiling coefficients in microchannels as the controlling mechanism is not nucleate boiling nor turbulent convection but is transient thin film evaporation (also, microchannel flows are typically laminar and not turbulent as assumed by macroscopic models). A more advanced three-zone flow boiling model for evaporation of elongated bubbles in microchannels is currently under development that so far qualitatively describes all these trends. Numerous fundamental aspects of two-phase flow and evaporation remain to be better understood and some of these aspects are also discussed.}, added-at = {2012-11-01T17:52:33.000+0100}, author = {Thome, John R.}, biburl = {https://www.bibsonomy.org/bibtex/21c3a626e37b8899437b701ca2a658603/thorade}, description = {ScienceDirect.com - International Journal of Heat and Fluid Flow - Boiling in microchannels: a review of experiment and theory}, doi = {10.1016/j.ijheatfluidflow.2003.11.005}, interhash = {d2b84ba4a4784a43c289ddb7242bf17f}, intrahash = {1c3a626e37b8899437b701ca2a658603}, issn = {0142-727X}, journal = {International Journal of Heat and Fluid Flow}, keywords = {2004 boiling experiment micro-channel review theory}, note = {Selected Papers from the 5th ECI International Conference on Boiling Heat Transfer}, number = 2, pages = {128 - 139}, timestamp = {2012-11-01T17:52:33.000+0100}, title = {Boiling in microchannels: a review of experiment and theory}, url = {http://dx.doi.org/10.1016/j.ijheatfluidflow.2003.11.005}, volume = 25, year = 2004 }