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- W2167671608 abstract "Recent experimental studies of evaporation in microchannels have shown that local flow-boiling coefficients are almost independent of vapor quality, weakly dependent on mass flux, moderately dependent on evaporating pressure, and strongly dependent on heat flux. In a conventional (macrochannel) geometry, such trends suggest nucleate boiling as the dominant heat transfer mechanism. In this paper, we put forward a simple new heat transfer model based on the hypothesis that thin-film evaporation into elongated bubbles is the important heat transfer mechanism in these flows. The new model predicts the above trends and quantitatively predicts flow-boiling coefficients for experimental data with several fluids. The success of this new model supports the idea that thin-film evaporation into elongated bubbles is the important heat transfer mechanism in microchannel evaporation. The model provides a new tool for the study of such flows, assists in understanding the heat transfer behavior, and provides a framework for predicting heat transfer." @default.
- W2167671608 created "2016-06-24" @default.
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- W2167671608 date "2002-12-01" @default.
- W2167671608 modified "2023-10-03" @default.
- W2167671608 title "Heat Transfer Model for Evaporation of Elongated Bubble Flows in Microchannels" @default.
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- W2167671608 doi "https://doi.org/10.1115/1.1517274" @default.
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