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Multiphase flow mixture in 180[degrees] pipe bends

Treść / Zawartość
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
This paper presents the results of research regarding measurements of the values of pressure drops during horizontal flow of gas-liquid and gas-liquid-liquid mixture through 180o pipe bends. The conducted insightful analysis and assessment during multi-phase flow in pipe bends has enabled to develop a new method for determination of their values. This new method for determining pressure drops ensures higher precision of calculation in comparison to other methods presented in literature and can be applied for calculation of these parameters during multi-phase flows in pipe bends with various geometries.
Rocznik
Strony
227--239
Opis fizyczny
Bibliogr. 18 poz., rys., tab.
Twórcy
autor
  • Opole University of Technology, Department of Chemical and Process Engineering, ul. Mikołajczyka 5, 45-271 Opole, Poland
autor
  • Opole University of Technology, Department of Chemical and Process Engineering, ul. Mikołajczyka 5, 45-271 Opole, Poland
Bibliografia
  • 1. Azzi A., Friedel L., Belaadi S., 2000. Two-phase flow pressure loss in bends. Forschung im Ingeniueurwesen, 65, 309-318. DOI: 10.1007/s100100000030.
  • 2. Chisholm D., 1967. A theoretical basis for the Lockhart-Martinelli correlation for two-phase flow. Int. J. Heat Mass Trans., 10, 1767-1778. DOI: 10.1016/0017-9310(67)90047-6.
  • 3. Chisholm D., 1980. Two-phase flow in bends. Int. J. Multiphase Flow, 6, 363-367. DOI: 10.1016/03019322(80)90028-2.
  • 4. Chisholm D., 1985. Two phase flow in heat exchangers and pipelines. Heat Trans. Eng., 6, 48-57. DOI: 10.1080/01457638508939624.
  • 5. Chen I.Y., Won C.L., Wang C.C., 2005. Influence of oil on R-410A two-phase frictional pressure drop in small U-type wavy tube. Int. Commun. Heat Mass Trans., 32, 797-808. DOI: 10.1016/j.icheatmasstransfer.2004.10.008.
  • 6. Domanski P.A., Hermes C.J.L., 2008. An improved correlation for two-phase pressure drop of R-22 and R-410A in 180[degrees] return bends. Appl. Therm. Eng., 28, 793-800. DOI: 10.1016/j.applthermaleng.2007.06.034.
  • 7. Dyga R., Nowak M., Troniewski L., 2006. Pressure losses for gas-liquid-liquid up-flow. Inż. Ap. Chem., 6S, 5758 (in Polish).
  • 8. Geary D.F., 1975. Return bend pressure drop in refrigeration systems. ASHRAE Trans., 32, 250-256.
  • 9. Hapanowicz J., 2001. Two-phase air-water flow in pipe bends. Inż. Chem. Proc., 22, 219-237.
  • 10. Hapanowicz J., Troniewski L., 1998. Pressure drops in two-phase liquid-liquid flow. Inż. Chem. Proc., 19, 531549 (in Polish).
  • 11. Nowak M., 2005. Modelling of three-phase water-air-oil flow in aspect of transportation of petroleum. ICSO Blachownia, Kędzierzyn-Koźle (in Polish).
  • 12. Pendyk B., 2002. Void fractions of gas-liquid-liquid three-phase flow in horizontal channels. PhD Thesis, Opole. (in Polish).
  • 13. Stomma Z., 1979. Two-phase flows – void fraction values determination. Report INR/18187/IXD/R/A, Institute of Nuclear Research, Świerk/Warszawa.
  • 14. Sookprasong P., 1980. Two-phase flow in piping components. MSc Thesis, University of Tulsa.
  • 15. Troniewski L., Dyga R., Nowak M., 2006. The decrease of pressure drop during the flow of a three-phase mixture. 17th International Congress of Chemical and Process Engineering CHISA, 3, 792-794.
  • 16. Ulbrich R., Witczak S., 1990. Two-phase flow in curved pipes. Multiphase Transport and Particulate Phenomena, 2, 65-78.
  • 17.Usui K., Aoki S., Inoue A., 1983. Flow behavior and phase distribution in two-phase flow around inverted Ubend. J. Nucl. Sci. Technol., 20, 915-928. DOI: 10.1080/18811248.1983.9733489.
  • 18. Yu Q.G., Barrier D., Cognet G., 1989. Two-phase flow in horizontal and vertical C-types bend- Pressure and void fraction distribution. European Two-Phase Flow Group Meeting, Paris.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-ecad4ff6-c2dd-467e-a3c6-d12ff8f75368
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