Pressure drop correlations for two-phase flow within horizontal rectangular channels with small heights
By H. Lee, Sang Yong Lee. 2001
361 citations recorded by the source corpus.
Subfields: Biomedical Engineering, Computational Mechanics, Mechanical Engineering
View Paper: https://www.semanticscholar.org/paper/4d6dba6d0b760bfff8b535fcbce88bffb23e3b4b
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In Biomedical Engineering
In Computational Mechanics
In Mechanical Engineering
Citations in the corpus
- Universal approach to predicting two-phase frictional pressure drop for adiabatic and condensing mini/micro-channel flows (2012, methodology): “The correlations of Yan and Lin [65] and Lee and Lee [66] show significant scatter, with MAE values of 178.0%, and 101.6%, respectively.”
- Fundamental issues related to flow boiling in minichannels and microchannels (2002, methodology): “Lee [43,44] R-113 G 1⁄4 50–200, q 1⁄4 3–15 kW/m(2) Rectangular 0.”
- Correlations of two-phase frictional pressure drop and void fraction in mini-channel (2010, background): “/ Lee and Lee [23] Adiabatic Rectangular duct 0.”
- Two-Phase Microchannel Heat Sinks: Theory, Applications, and Limitations (2011, neutral): “Consequently, two-phase pressure drop and heat transfer models for the microchannel evaporator are based mostly on these regimes [59] [60] [61] [62] [63] [64] [65].”
- Universal approach to predicting two-phase frictional pressure drop for mini/micro-channel saturated flow boiling (2013, background): “[50], (f) Lee and Lee [51], (g) Yu et al.”
- Two-phase flow in high-heat-flux micro-channel heat sink for refrigeration cooling applications: Part II—heat transfer characteristics (2005, neutral): “:3 vgvf 0:4 ;Wefo ¼ vfG 2dh r Small channel correlation 6 Lee and Lee (2001) [12] htp ¼ Nu3 Nu4 ðEhspÞ Small channel correlation hsp ¼ Nu kf dh ; Nulam ¼ constðRefer to Eqs: (7) and (8)Þ; Nutur ¼ 0:023Re0:8f Pr0:4f E ¼ 10:3b0:398/0:598f ;/ 2 f ¼ 1þ C X þ 1 X 2 ;C ¼ 6:185 10 2Re0:726fo X 2 ¼…”
- Flow boiling of water in a circular staggered micro-pin fin heat sink (2008, background): “Rapid bubble growth [33–35], different dependency, than in conventional scale, of the heat transfer coefficient on heat flux [9,31,36,37], mass flux, and quality [7,9], increased heat flux at the onset of nucleate boiling [7], and length scale dependency of the two-phase frictional multiplier [26,29”