MODELS FOR HEAT TRANSFER CALCULATION DURING FILM CONDENSATION INSIDE HORIZONTAL TUBES

Keywords: heat transfer, condensation, film, model, horizontal tube.

Abstract

The study of heat transfer during condensation in the middle of the pipes is relevant due to the constant need to improve the design of various heat exchangers (condensers of refrigeration and air conditioning systems, reactor safety systems, and power plant heaters). It is important to know the exact values of heat transfer coefficients in the case of condensation when their value is close to the heat transfer from the cooling side. Well-known theoretical, semi-empirical and experimental models and correlations for heat transfer calculation during condensation of working fluids inside smooth horizontal pipes have been described in the article. Selected models are widely used in various scientific publications for heat transfer prediction and construction of various heat exchangers with in-tube condensation. All correlations allow determining the average by tube perimeter, but local by the length of the tube, heat transfer coefficients in the case of annular and intermediate regimes of two-phase flow. All used dependences take into account current modes of phase flow. For choosing the best correlations, a comparison between selected models and experimental values of heat transfer coefficients obtained by different authors for condensation of ten working fluids inside smooth horizontal tubes with internal diameters more than 3 mm have been performed. Experimental values were selected from well-known works, in which heat transfer was studied during condensation of such fluids as fluorocarbons, immersion refrigerants, hydrocarbons and steam in the case of intermediate and annular phase flows with a detailed description of research conditions (geometrical parameters of investigated tubes and regimes parameters of condensation process, such as heat flux, mass velocity, vapour quality, and condensation temperature). Comparison of various models with experimental data of different authors allowed identifying the models that show the best convergence with experiments among all correlations. Recommendations (range of application) for use of models in engineering practice are given.

Downloads

Download data is not yet available.

| Abstract views: 98 | PDF Downloads: 47 |

References

Doretti L., Zilio C., Mancin S., Cavallini A. Condensation Flow Patterns inside plain and Microfin Tubes: A Review. International Journal of Refrigeration. 2013. Vol. 36, № 2. pp. 567-587.

Dalkilic A, Aktas M, Acikgoz O, Wongwises S. A Review of Recent Empirical Correlations for the Calculation of Determination of R134a’s Convective Heat Transfer Coefficient in Vertical Condensers. International Communications in Heat and Mass Transfer. 2015. № 69. pp. 41-50.

Huang J, Zhang J, Wang L. Review of vapor condensation heat and mass transfer in the presence of non-condensable gas. Applied Thermal Engineering. 2015. № 89. pp. 469-484.

Righetti G, Zilio C, Mancin S, Longo G. A review on in-tube two-phase heat transfer of hydro-fluoro-olefines refrigerants. Science and Technology for the Built Environment. 2016. Vol. 22. № 8. pp. 1191-1225.

Rifert V, Gorin V, Usenko V, Sereda V. Condensation inside horizontal pipes: the state of the issue and analysis of the research problem. Industrial heat engineering. 2011. № 33 (8). pp. 62-71.

Rifert V, Barabash P, Gorin V, Sereda V. Heat transfer by condensation inside horizontal smooth pipes. Improving the method of calculat-ing heat exchange. Refrigeration equipment and technology. 2015. № 6 (51). pp. 26-34.

Sereda V, Gorin V. Hydrodynamics and heat exchange during condensation of working steam in the middle of horizontal pipes in the case of stratified phase flow regime. Calculation of heat transfer. Integrated technologies and energy saving. 2018. № 4. pp. 48-56.

Fujii T. Enhancement to condensing heat transfer – new developments. Journal of En-hanced Heat Transfer. 1995. № 2. pp. 127-137.

Thome J. R., Hajal J., Cavallini A. Condensation in horizontal tubes. Part 2: New heat transfer model based on flow regimes. International Journal of Heat and Mass Transfer. 2003. Vol. 46. № 18. pp. 3365-3387.

Jassim E. W., Newell T. A., Chato J. C. Prediction of two-phase condensation in horizontal tubes using probabilistic flow regime maps. International Journal of Heat and Mass Transfer. 2008. Vol. 51. № 3. pp. 485-496.

Cavallini A., Del Col D., Doretti L., Matkovic M., Rossetto L., Zilio C., Censi G. Condensation in Horizontal Smooth Tubes: A New Heat Transfer Model for Heat Exchanger Design. Heat Transfer Engineering. 2006. Vol. 27. № 8. pp. 31-38.

Ananiev E. P., Boyko L. D., Kruzhilin G. N. Heat transfer in the presence of steam condensation in a horizontal tube. Proceedings of the 2nd International Heat Transfer Conference. August Colorado. Part 2. 1961. pp. 290-295.

Shah M. M. A general correlation for heat transfer during film condensation inside pipes. International Journal of Heat and Mass Transfer. 1979. Vol. 22. № 4. pp. 547-556.

Shah M. M. General correlation for heat transfer during condensation in plain tubes: Fur-ther development and verification. ASHRAE Transactions. 2013. Vol. 119. № 2. pp. 1-9.

Shah M. M. Prediction of Heat Transfer during Condensation in Non-Circular Channels. Inventions. Engineering Research As-sociates. 2019. pp. 1-22.

Traviss D. P., Baron A.B., Rohsenow W. M. Forced-convection condensation inside tubes. Report No. DSR-72591-74. Massachusetts Institute of Technology. Cambridge. MA. 1971. 105 p.

Zivi S. M. Estimation of steady-state steam void-fraction by means of the principle of minimum entropy production. Transactions of the ASME. 1975. № 86. pp. 247-252.

Rouhani S. Z. Subcooled void fraction, Report No. AE-RTV841. AB Atomenergi Sweden, 1969. 138 p.

Dittus F. W., Boelter L. M. K. Heat Transfer in Automobile Radiators of the Tubular Type. University of California Press. Berkeley. University of California Publications in Engineer-ing. 1930. Vol. 2. 443-461.

Chato J. Laminar condensation inside horizontal and inclined tube. ASHRAE Journal. 1962. Vol. 4. № 2. pp. 52-60.

Dobson M., Chato J. Condensation in smooth horizontal tubes. Journal of Heat Trans-fer of ASME. 1998. Vol. 120. № 1. pp. 193–213.

Kim Y. J., Jang J., Hrnjak P. S., Kim M. S. Condensation heat transfer of carbon dioxide inside horizontal smooth and microfin tubes at low temperature. Journal of Heat Trans-fer of ASME. 2009. Vol. 131. № 2. pp. 1-10.

Park K. J., Jung D., Seo T. Flow condensation heat transfer characteristics of hydrocarbon refrigerants and dimethyl ether inside a horizontal plain tube. Journal of Multiphase Flow. 2008. Vol. 34. № 7. pp. 628-635.

Ghim G., Lee J. Condensation heat trans-fer of low GWP ORC working fluids in a hori-zontal smooth tube. International Journal of Heat and Mass Transfer. 2017. Vol. 104. pp. 718-728.

Lee H., Mudawar І., Hasan M. Flow condensation in horizontal tubes. International Journal of Heat and Mass Transfer. 2013. № 66. pp. 31-45.

Boyko L. D. Heat transfer during vapor condensation inside tubes (in Russian). Heat Transfer in the Elements of Power Plants. 1966. pp. 197-212.

Cavallini A., Censi G., Del Col D., Doret-ti L., Longo G. A., Rossetto L. Experimental in-vestigation on condensation heat transfer and pressure drop of new refrigerants (R134a, R125, R32, R410A, R236ea) in a horizontal smooth tube. International Journal of Refrigeration. 2001. Vol. 24. № 1. pp. 73-87.

Published
2021-09-24
How to Cite
[1]
V. V. Gorin, L. V. Kolomiets, and V. V. Sereda, “MODELS FOR HEAT TRANSFER CALCULATION DURING FILM CONDENSATION INSIDE HORIZONTAL TUBES”, Збірник наукових праць Одеської державної академії технічного регулювання та якості, no. 1(18), pp. 31-40, Sep. 2021.