Summary
A series of experiments are conducted to investigate the two-phase pressure drop of ammonia in horizontal small diameter tube. The experiments are performed at saturation temperatures of -15.8–4.6 °C, and the mass flux range is from 20 to 100?kg m-2 s-1. This paper analyzes the influence mechanisms of vapor quality, mass flux, saturation temperature, and tube diameter on the two-phase frictional pressure gradient in detail. Meanwhile, several correlations are compared with all the experimental data and the results show that the Müller-Steinhagen and Heck (1986) correlation gives the best agreement. With the analysis of the major forces for ammonia two-phase flow under the tested experimental conditions, the Reynolds number and Bond number are introduced to modify the Müller-Steinhagen and Heck (1986) correlation. Lastly, a modified correlation is developed with the mean absolute deviation of only 13.5%, and 89.2% of the data are within the?±?30% error band. In addition, the modified correlation is evaluated based on a complied database which contains 951 experimental data points from 11 published literatures.
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Details
- Original title: Two-phase pressure drop of ammonia in horizontal small diameter tubes: Experiments and correlation.
- Record ID : 30025389
- Languages: English
- Source: International Journal of Refrigeration - Revue Internationale du Froid - vol. 98
- Publication date: 2019/02
- DOI: http://dx.doi.org/10.1016/j.ijrefrig.2018.11.018
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Indexing
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Themes:
Ammonia;
Two-phase flow - Keywords: Two-phase flow; Horizontal tube; Correlation; Temperature; R717; Ammonia; Prediction; Expérimentation; Pressure drop
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- Source: 16th IIR-Gustav Lorentzen Conference on Natural Refrigerants (GL2024). Proceedings. University of Maryland, College Park, Maryland, USA, August 11-14 2024
- Formats : PDF
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