Condensation heat transfer and pressure drop of HFC-134a in a helically coiled concentric tube-in-tube heat exchanger
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Garimella, 1988, Experimental investigation of heat transfer in coiled annular duct, Trans. ASME, 110, 329, 10.1115/1.3250488
Xin, 1997, An experimental study of single-phase and two-phase flow pressure drop in annular helicoidal pipes, Int. J. Heat Fluid Flow, 18, 482, 10.1016/S0142-727X(97)00033-7
Kang, 2000, Condensation of R-134a flowing inside helicoidal pipe, Int. J. Heat Mass Transfer, 43, 2553, 10.1016/S0017-9310(99)00296-3
T.J. Rennie, G.S.V. Raghavan, Laminar parallel flow in a tube-in-tube helical heat exchanger, the AIC 2002 Meeting CSAE/SCGR Program Saskatoon, Saskachewan, Paper No. 02-406, 2002.
Yu, 2003, Condensation heat transfer of R-134a flow inside helical pipes at different orientations, Int. Commun. Heat Mass Transfer, 30, 745, 10.1016/S0735-1933(03)00122-2
W.I. Louw, J.P. Meyer, Annular tube contact in a helically coiled tube-in-tube heat exchanger, in: Proceedings of the 2nd International Conference on Heat Transfer, Fluid Mechanics and Thermodynamics, Victoria Falls, Zambia, 23–26 June, 2003.
Murai, 2005, Backlight imaging tomography for gas–liquid two-phase flow in a helically coiled tube, Measur. Sci. Technol., 16, 1459, 10.1088/0957-0233/16/7/008
Rennie, 2005, Experimental studies of a double-pipe helical heat exchanger, Exp. Thermal Fluid Sci., 29, 919, 10.1016/j.expthermflusci.2005.02.001
M.O. McLinden, S.A. Klein, E.W. Lemmon, REPROP, Thermodynamic and transport properties of refrigerants and refrigerant mixtures. NIST Standard Reference Database-version 6.01, 1998.
Chisholm, 1973, Pressure gradients due to friction during the flow of evaporating two-phase mixtures in smooth tubes and channels, Int. J. Heat Mass Transfer, 16, 347, 10.1016/0017-9310(73)90063-X
Breber, 1980, Prediction of horizontal tube-side condensation of pure components using flow regime criteria, J. Heat Transfer, 102, 471, 10.1115/1.3244325
Cavallini, 2001, Experimental investigation on condensation heat transfer and pressure drop of new HFC refrigerants (R134a, R125, R32, R410A, R236ea) in a horizontal smooth tube, Int. J. Refrig., 24, 73, 10.1016/S0140-7007(00)00070-0
Nualboonrueng, 2003, Two-phase condensation heat transfer coefficients of HFC-134a at high mass flux in smooth and micro-fin tubes, Int. Commun. Heat Mass Transfer, 30, 577, 10.1016/S0735-1933(03)00086-1
Owhadi, 1968, Forced convection boiling inside helically-coiled tubes, Int. J. Heat Mass Transfer, 11, 1779, 10.1016/0017-9310(68)90021-5
Jung, 2003, Flow condensation heat transfer coefficients of pure refrigerants, Int. J. Refrig., 26, 4, 10.1016/S0140-7007(02)00082-8
A. Cavallini, R. Zecchin, A dimensionless correlation for heat transfer in forced convection condensation, in: Proceedings of the 6th International Heat Transfer Conference, Tokyo, pp. 309–313, 1997.
L. Tang, Empirical study of new refrigerant flow condensation inside horizontal smooth and micro-fin tubes, Ph.D. Thesis, University of Maryland, 1997.
Nualboonrueng, 2004, Two-phase flow pressure drop of HFC-134a during condensation in smooth and micro-fin tubes at high mass flux, Int. Commun. Heat Mass Transfer, 31, 991, 10.1016/j.icheatmasstransfer.2004.05.009
Lockhart, 1949, Proposed correlation of data for isothermal two-phase two-component flow in pipes, Chem. Eng. Prog., 45, 39
Ito, 1959, Frictional factor for turbulent flow in curved pipes, Trans. ASME, J. Basic Eng., 81, 123, 10.1115/1.4008390
Chisholm, 1967, A theoretical basis for the Lockhart–Martinelli correlation for two-phase flow, Int. J. Heat Mass Transfer, 10, 1767, 10.1016/0017-9310(67)90047-6