IIR document
Prediction of evaporative heat transfer coefficient of pure refrigerants and binary refrigerant mixtures in a horizontal tube.
Author(s) : HONG E. C., KIM M. S., RO S. T.
Summary
Evaporative heat transfer coefficient was predicted for an annular flow of pure refrigerants and non-azeotropic binary refrigerant mixtures inside a horizontal tube. The heat transfer coefficients of pure refrigerants are predicted within more or less 14% error bound compared with the available experimental data. The calculation model applied to predict the heat transfer coefficients of non-azeotropic binary refrigerant mixtures shows a standard deviation of more or less 18%. Properties of refrigerant mixtures were calculated for several cases considering the composition difference in vapour and liquid phases, and the nonlinearity in the mixing rules. Results are given.
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Details
- Original title: Prediction of evaporative heat transfer coefficient of pure refrigerants and binary refrigerant mixtures in a horizontal tube.
- Record ID : 1996-0791
- Languages: English
- Source: For a Better Quality of Life. 19th International Congress of Refrigeration.
- Publication date: 1995/08/20
- Document available for consultation in the library of the IIR headquarters only.
Links
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Indexing
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Themes:
Mass transfer;
Blends - Keywords: Horizontal tube; Heat transfer coefficient; Calculation; Heat transfer; Simulation; Binary mixture; Refrigerant; Boiling
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