New flow boiling heat transfer model and flow pattern map for carbon dioxide evaporating inside horizontal tubes
By Lixin Cheng, Gherhardt Ribatski, L. Wojtan, John Richard Thome. 2006
179 citations recorded by the source corpus.
Subfields: Mechanical Engineering
View Paper: https://www.semanticscholar.org/paper/5f9c66c04104418b348cadb1d333cec3d5e1691d
How researchers see this paper
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In Mechanical Engineering
- Sung-Min Kim
- I. Mudawar
- Gherhardt Ribatski
- Lixin Cheng
- John Richard Thome
- J. Quibén
- Satish G. Kandlikar
- Suresh V. Garimella
Citations in the corpus
- Universal approach to predicting saturated flow boiling heat transfer in mini/micro-channels - Part II. Two-phase heat transfer coefficient (2013, unknown): “[66,68] are modified versions of those of Wojtan et al.”
- New Prediction Methods for CO2 Evaporation Inside Tubes: Part II - An Updated General Flow Boiling Heat Transfer Model Based on Flow Patterns (2008, methodology): “Corresponding to the updated flow pattern map presented in part I of this study, a general flow pattern based flow boiling heat transfer model was developed for CO2 on the basis of the Cheng-Ribatski-Wojtan-Thome flow boiling heat transfer model [1].”
- Universal approach to predicting saturated flow boiling heat transfer in mini/micro-channels – Part I. Dryout incipience quality (2013, background): “[66,68] are modified versions of those of Wojtan et al.”
- New prediction methods for CO2 evaporation inside tubes: Part I – A two-phase flow pattern map and a flow pattern based phenomenological model for two-phase flow frictional pressure drops (2008, methodology): “However, none of these is applicable to CO2 evaporation in horizontal tubes because the two-phase flow characteristics of CO2 evaporation are greatly affected by the very high pressures and low surface tensions of CO2 [1, 10].”