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- W2014966315 abstract "ABSTRACT:Characteristics of flow boiling heat transfer in microchannels were investigated experimentally. The microchannels consisted of 9 parallel trapezoidal channels with each channel having 205 m of bottom width, 800 m of depth, 3.6 o of sidewall angle, and 7 cm of length. Tests were performed with R113 over a mass velocity range of 150~920 kg/m 2 s, heat flux of 10~100 kW/m 2 and inlet pressures of 105~195 kPa. Flow boiling heat transfer coefficient in microchannels was found to be dominated by heat-flux. However the effect of mass velocity was not significant. Contrary to macrochannel trends, the heat transfer coefficient was shown to decrease with increa-sing thermodynamic equilibrium quality. A new correlation suitable for predicting flow boiling heat transfer coefficient was developed based on the laminar single-phase heat transfer coefficient and the nucleate boiling dominant equation. Comparison with the experimental data showed good agreement.Keywords:Flow boiling heat transfer(유동비등 열전달), Microchannels(미세유로), Quality(건도), Boiling number(비등 수), Martinelli parameter(마티넬리 변수)" @default.
- W2014966315 created "2016-06-24" @default.
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- W2014966315 date "2011-11-10" @default.
- W2014966315 modified "2023-09-23" @default.
- W2014966315 title "Convective Boiling Two-phase Flow in Trapezoidal Microchannels : Part 2-Heat Transfer Characteristics" @default.
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- W2014966315 doi "https://doi.org/10.6110/kjacr.2011.23.11.718" @default.
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