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An improved Müller-Steinhagen and Heck model for two phase pressure drop modeling at high reduced pressures

Wybrane pełne teksty z tego czasopisma
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Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
Better understanding of two-phase fluid behavior is required to optimize the design models of the components containing a twophase refrigerant. This is important since applications increasingly seek to operate in the region of high reduced pressure values, for instance the vapor generator, which is a key heat exchanger in the Organic Rankine Cycle system and the high temperature heat pump. Implementations are carried out at high evaporation saturation temperatures where the refrigerant transformation to vapor occurs at temperatures higher than 90°C. Analysis of the literature analysis shows there is a gap in knowledge regarding two-phase flow for synthetic refrigerants at high saturation temperatures. Reliable prediction of pressure drop in two-phase flows is an important prerequisite for accurate optimization of thermal systems. The total pressure drop of a fluid derives from the variation of potential and kinetic energy of the fluid and friction on the channel walls or between the phases (60-120oC) and moderate reduced pressures (0.2-0.5). This paper presents a modification to the established Müller-Steinhagen and Heck (1986) model for two phase pressure drop in relation to high values of reduced pressures. Model validation has been done in comparison to reliable experimental data obtained by Charnay et al. (2015) for R245fa at reduced pressures above 0.5. The modification constitutes a significant improvement on the calculations presented in the literature, including by the authors of experimental data.
Rocznik
Strony
81--87
Opis fizyczny
Bibliogr. 19 poz., wykr.
Twórcy
  • Gdańsk University of Technology, Faculty of Mechanical Engineering and Ship Technology, Institute of Energy, Narutowicza 11/12, 00-233 Gdańsk, Poland
  • Institute of Fluid-Flow Machinery PAS, Fiszera 14, 00-231 Gdańsk, Poland
Bibliografia
  • [1]. Cavallini A, Censi G, Del Col D, Doretti L, Longo G A, Rossetto L. Condensation of Halogenated Refrigerants Inside Smooth Tubes. HVAC and Research, vol. 8, no. 4, 429–451, 2002.
  • [2]. Carey VP. Liquid-vapor phase-change phenomena: an introduction to the thermophysics of vaporization and condensation processes in heat transfer equipment. Hemisphere Publishing, Washington (DC) 1992.
  • [3]. Charnay R, Revellin R, Bonjour J, Discussion on the validity of prediction tools for two-phase flow pressure drops from experimental data obtained at high saturation temperatures. Int. Journal of Refrigeration, 54, 98-125, 2015.
  • [4]. Chisholm D. Pressure gradients due to friction during the flow of evaporating two-phase mixtures in smooth tubes and channels. Int. J. Heat Mass Transfer, 16, 347-358, 1973.
  • [5]. Del Col D, Bisetto A, Bortolato M, Torresin D, Rossetto L. Experiments and updated model for two phase frictional pressure drop inside minichannels. Int. Journal of Heat and Mass Transfer, 67, 326-337, 2013.
  • [6]. Friedel L. Improved Friction Pressure Drop Correlations for Horizontal and Vertical Two-Phase Pipe Flow. Proc. European Two-Phase Flow Group Meeting, Paper E2, Ispra, Italy, 1979.
  • [7]. Jakubowska B, Mikielewicz D. An Improved Method for Flow Boiling Heat Transfer with Account of the Reduced Pressure Effect, Thermal Science, 23, Suppl. 4, 1261-1272, 2019.
  • [8]. Kew PA, Cornwell K. Correlations for the Prediction of Boiling Heat Transfer in Small Diameter Channels. Applied Thermal Eng, 17(8-10), 705-715, 1997.
  • [9]. Lockhart RW, Martinelli RC. Proposed correlation of data for isothermal two-phase two-component flow in pipes. Chemical Engineering Progress, 45, 39-45, 1949.
  • [10]. Mikielewicz D, Jakubowska B. Calculation method for flow boiling and flow condensation of R134a and R1234yf in conventional and small diameter channels. Polish Maritime Research, 24, SI(93), 141-148, 2017.
  • [11]. Mikielewicz D, Mikielewicz J. A common method for calculation of flow boiling and flow condensation heat transfer coefficients in minichannels with account of nonadiabatic effects. Heat Transfer Eng., 32, 1173-1181, 2011.
  • [12]. Mikielewicz D. A new method for determination of flow boiling heat transfer coefficient in conventional diameter channels and minichannels. J. of Heat Transfer Eng., 31, 276-287, 2010.
  • [13]. Mikielewicz D, Mikielewicz J, Białas-Tesmar J. Improved semi-empirical method for determination of heat transfer coefficient in flow boiling in conventional and small diameter tubes. Int. Journal of Heat and Mass Transfer, 50(19-20), 3949-3956, 2007.
  • [14]. Mikielewicz D, Jakubowska B, Prediction of flow boiling heat transfer coefficient for carbon dioxide in minichannels and conventional channels. Arch. of Thermodynamics, 37(2), 89-106, 2016.
  • [15]. Mikielewicz D, Andrzejczyk R, Jakubowska B, Mikielewicz J. Comparative study of heat transfer and pressure drop during flow boiling and flow condensation in minichannels. Archives of Thermodynamics, 35(2), 17-37, 2014.
  • [16]. Mikielewicz D, Jakubowska B. Prediction of flow boiling heat transfer data for R134a, R600a and R290 in minichannels. Arch. of Thermodynamics, 35(4), 97-114, 2014.
  • [17]. Müller-Steinhagen H, Heck K. A simple friction pressure drop correlation for two-phase flow in pipes. Chem. Eng. Process Intensification 20(6), 297-308, 1986.
  • [18]. Tran TN, Chyu M-C, Wambsganss MW, France DM. Two-Phase Pressure Drop of Refrigerants During Flow Boiling in Small Channels: An Experimental Investigation and Correlation Development. Int. Journal of Refrigeration, 26(11), 1739-1754, 2000.
  • [19]. Zhang M, Webb RL, Correlation of Two-phase Friction for Refrigerants in Small-Diameter Tubes. Exp. Therm. Fluid Sci., 25(3-4), 131-139, 2001.
Uwagi
PL
Opracowanie rekordu ze środków MEiN, umowa nr SONP/SP/546092/2022 w ramach programu "Społeczna odpowiedzialność nauki" - moduł: Popularyzacja nauki i promocja sportu (2022-2023).
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-760637ec-d254-4aa1-acdb-54d4053d19ab
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