Flow boiling heat transfer of Freon R11 and HCFC123 in narrow passages
By Z. Bao, D. Fletcher, B. Haynes. 2000
321 citations recorded by the source corpus.
Subfields: Computational Mechanics, Mechanical Engineering
View Paper: https://www.semanticscholar.org/paper/bfc55728ea0989b5400d7af2e231d950eeecf159
How researchers see this paper
The researchers whose trusted networks rank it highest, strongest advocate first. Every researcher gets a different order.
In Computational Mechanics
- Suresh V. Garimella
- I. Mudawar
- S. Bertsch
- Eckhard A. Groll
- Yoav Peles
- Ali Kosar
- Jaeseon Lee
- Satish G. Kandlikar
In Mechanical Engineering
- Suresh V. Garimella
- Satish G. Kandlikar
- I. Mudawar
- S. Bertsch
- Eckhard A. Groll
- Yoav Peles
- T. Harirchian
- Ali Kosar
Citations in the corpus
- Effects of heat flux, mass flux, vapor quality, and saturation temperature on flow boiling heat transfer in microchannels (2009, background): “For example, Bao, Fletcher, and Haynes (2000) and Lazarek and Black (1982) reported an almost constant heat transfer coefficient with respect to thermodynamic vapor quality for flow boiling in microchannels.”
- Review and Comparative Analysis of Studies on Saturated Flow Boiling in Small Channels (2008, background): “(2000) [32] R11, R123 in copper circular D = 1.”
- Flow boiling in microchannels: Fundamentals and applications (2017, background): “A group of researchers, such as [53,54], concluded that nucleate boiling is the dominant heat transfer mechanism.”
- State-of-the-Art Overview of Boiling and Two-Phase Flows in Microchannels (2006, background): “[40] for R123 at 335 kg/m2s, 86 kW/m2, and channel diameter of 1.”
- Flow boiling heat transfer in two-phase micro-channel heat sinks––I. Experimental investigation and assessment of correlation methods (2003, background): “As shown in Table 1, a few investigators indicated the dominant heat transfer mechanism for mini-channels is nucleate boiling, based largely on a strong dependence of the heat transfer coefficient on heat flux and a weaker dependence on G and xe [7,10,11,16].”
- Effect of tube diameter on boiling heat transfer of R-134a in horizontal small-diameter tubes (2005, background): “[4] studied boiling flow of refrigerants R-11 and R-123 in a 1.”
- Boiling heat transfer in a hydrofoil-based micro pin fin heat sink (2007, methodology): “The single-phase heat transfer coefficient is found using existing correlations like Zukauskas [36], while the nucleate boiling heat transfer coefficient is typically obtained through a power law relation [22,86, 104–108]”
- Universal approach to predicting saturated flow boiling heat transfer in mini/micro-channels - Part II. Two-phase heat transfer coefficient (2013, unknown): “To achieve this goal, published saturated flow boiling heat transfer databases for mini/micro-channel flows are amassed from 37 sources [26–62].”
- Two-phase flow in high-heat-flux micro-channel heat sink for refrigeration cooling applications: Part II—heat transfer characteristics (2005, background): “The first shares the view that nucleate boiling is dominant and therefore dictates overall heat transfer inside the channel, citing the local heat transfer coefficient is dependent on heat flux, but not mass velocity or quality [3,4,6,10,11,14].”