Abstract
An experimental investigation on the flow pattern and pressure drop was carried out for both an adiabatic and a diabatic two-phase flow in a horizontal tube with pure refrigerants R134a and R123 and their mixtures as test fluids. The observed flow patterns were compared to the flow pattern map of Kattan et al., which predicted well the present data over the entire regions of mass velocity in this study. The measured frictional pressure drop in the adiabatic experiments increased with an increase in vapor quality and mass velocity. These data were compared to various correlations proposed in the past for the frictional pressure drop. The Chisholm correlation underpredicted the present data both for pure fluids and their mixtures in the entire mass velocity range of 150 to 600 kg/m2s covered in the measurements, while the Friedel correlation was found to overpredict the present data in the stratified and stratified-wavy flow region, and to underpredict in the annular flow region.
Similar content being viewed by others
Abbreviations
- D :
-
Tube inner diameter (m)
- f:
-
Friction factor
- g :
-
Mass velocity (kg/m2s)
- L :
-
Tube length (m)
- P :
-
Pressure drop (Pa)
- q :
-
Heat flux (W/m2)
- Re :
-
Reynolds number
- X :
-
Mole fraction in liquid
- Y :
-
Mole fraction in vapor
- z :
-
Axial distance (m)
- α:
-
Void fraction
- β :
-
Vapor quality
- ρ :
-
Density (kg/m3)
- ε :
-
Viscosity (Pa s)
- Ф :
-
Two-phase frictional multiplier
- a :
-
Acceleration
- f:
-
Friction
- fo :
-
Total flow assumed as liquid
- i :
-
Inlet of the heat transfer section
- l:
-
Liquid
- o :
-
Outlet of the heat transfer section
- TP :
-
Two-phase
- v :
-
Vapor
References
Barajas, A.M. and Panton, R. L., 1993, The Effects of Contact Angle on Two-Phase Flow in Capillary Tubes, Int. J. Multiphase Flow, Vol. 19, pp. 337–346.
Chisholm, D., 1973, Pressure Gradients Due to Friction During the Flow of Evaporating Two-Phase Mixtures in Smooth Tubes and Channels, Int. J. Heat Mass Transfer, Vol. 16, pp. 347–358.
Collier, J. G. and Thome, J. R., 1994, Convective Boiling and Condensation, 3rd Edition. Oxford University Press, London.
Friedel, L., 1979, Improved Friction Pressure Drop Correlations for Horizontal and Vertical Two-Phase Pipe Flow, Presented at the European Two-phsae Flow Group Meeting, Ispra, Italy, Paper E2, June, Vol. 18, pp. 485–492.
Hosier, E. R., 1968, Flow Patterns in High Pressure Two Phase (Steam-Water) Flow with Heat Addition, AIChE Symp. Ser. Vol. 64, pp. 54–66.
Jung, D.S. and Radermacher, R., 1989, Prediction of Pressure Drop During Horizontal Annular Flow Boiling of Pure and Mixed Refrigerants. Int. J. Heat Mass Transfer, Vol. 32, pp. 2435–2446.
Kattan, N., Thome, J. R. and Favrat, D., 1998 Flow Boiling in Horizontal Tubes, Part 1, J. Heat Transfer, Vol. 120, pp. 140–147.
Lockhart, R.W. and Martinelli, R. C., 1949, Proposed Correlation of data for Isothermal Two-Phase, Two-Component Flow in Pipes, Chem. Engng. Prog. Vol. 45, pp. 39–48.
Martinelli, R. C. and Nelson, D. B., 1948, Prediction of Pressure Drop During Forced-Circulation Boiling of Water, Trans. ASME Vol. 70. pp. 695–702.
Nishiumi, H. and Saito, S., 1977, Correlation of the Binary Interaction Parameter of the Modified Generalized BWR Equation of State, J. Chem. Eng. Japan, Vol. 10, pp. 176–180.
Pierre, B., 1966, Flow Resistance with Boiling Refrigerants, ASHRAE Trans., pp. 28–42.
Premoli, A., Francesco, D. and Prina, A., 1970, An Empirical Correlation for Evaluating Two-Phase Mixture Density Under Adiabatic Conditions, European Two-Phase Flow Group Meeting, Milan.
Reid, R. C., Prausnitz, J. M. and Sherwood, T. K., 1977, The Properties of Gases and Liquids, 3rd Edn., McGraw-Hill, New York.
Thom, J. R. S., 1964, Prediction of Pressure Drop During Forced Circulation Boiling of Water, Int. J. Heat Mass Transfer, Vol. 7, pp. 709–724.
VDI-Warmeatlas, 1993, Heat Transfer to Boiling Saturated Liquids, VDI Heat Atlas, Chapter Hbb1. Dusseldorf, Germany: VDI-Verlag GmbH (in English).
Whalley, P. B., 1987, Boiling, Condensation and Gas-Liquid Flow, Oxford University Press, New York.
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Lim, T.W., Han, K.I. A study on pressure drop characteristics of refrigerants in horizontal flow boiling. KSME International Journal 17, 758–765 (2003). https://doi.org/10.1007/BF02983871
Received:
Revised:
Published:
Issue Date:
DOI: https://doi.org/10.1007/BF02983871