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Pressure drop in two-phase gas-liquid (Taylor) flow in microreactors

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Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
The pressure drop in microreactors for the gas - liquid Taylor flow was measured for 4 different microreactor geometries and 3 different gas - liquid systems. The results have been compared with the existing literature correlations. A selection of the best correlations has been made.
Rocznik
Strony
369--384
Opis fizyczny
Bibliogr. 17 poz., tab., rys.
Twórcy
autor
autor
autor
  • Faculty of Chemical and Process Engineering, Warsaw University of Technology, Waryńskiego 1, 00-645 Warsaw, Poland
Bibliografia
  • 1. Abiev R.Sh., 2011. Modeling pf pressure losses for the slug flow of gas-liquid mixture in mili- and microchannels. Theor. Found. Chem. Eng., 45, 156-163. DOI: 10.1134/S0040579511020011.
  • 2. Bretherton F.P., 1961. The motion of long bubbles in tubes. J. Fluid Mech., 10, 166-188. DOI: 10.1017/S0022112061000160.
  • 3. Beattie D.R.H., Whalley P.B., 1982. A simple two-phase flow frictional pressure drop calculation method. Int. J. Multiph. Flow, 8, 83–87. DOI: 10.1016/0301-9322(82)90009-X.
  • 4. Chisholm D., 1967. A theoretical basis for the Lockhart-Martinelli correlation for two-phase flow. Int. J. Heat Mass Transfer., 10, 1767-1778. DOI: 10.1016/0017-9310(67)90047-6.
  • 5. Dukler A.E., Wicks III M., Cleveland R.G., 1964. Frictional pressure drop in two-phase flow: A. A comparison of existing correlations for pressure loss and holdup. AIChE J., 10, 38–43. DOI: 10.1002/aic.690100117.
  • 6. Dziubiński M., Prywer J., 2009. Mechanics of two phase fluids. WNT, Warsaw, 417-462 (in Polish).
  • 7. Fries D.M., Trachsel F., von Rohr P.R., 2008. Segmented gas–liquid flow characterization in rectangular microchannels. Int. J. Multiph. Flow, 34, 1108-1118. DOI: 10.1016/j.ijmultiphaseflow.2008.07.002.
  • 8. Kawahara A., Chung P.M.-Y., Kawaji M., 2002. Investigation of two-phase flow pattern, void fraction and pressure drop in a microchannel. Int. J. Multiph. Flow, 28, 1411–1435. DOI: 10.1016/S0301-9322(02)00037-X.
  • 9. Kreutzer M.T., van der Eijnden M.G., Kapteijn F., Moulijn J.A., Heiszwolf J.J., 2005a. The pressure drop experiments to determine slug lengths in multiphase monoliths. Catal. Today, 105, 667–672. DOI:10.1016/j.cattod.2005.06.007.
  • 10. Kreutzer M. T., Kapteijn F., Moulijn J. A., Kleijn C. R., Heiszwolf J. J., 2005b. Inertial and interfacial effects on pressure drop of Taylor flow in capillaries. AIChE J., 51, 2428-2440. DOI: 10.1002/aic.10495.
  • 11. Kreutzer M.T., Kapteijn F., Moulijn J.A., Heiszwolf J.J., 2005c. Multiphase monolith reactors: Chemical reaction engineering of segmented flow in microchannels. Chem. Eng. Sci., 60, 5895-5916. DOI:10.1016/j.ces.2005.03.022.
  • 12. Lee H.J., Lee S.Y., 2001. Pressure drop correlations for two-phase flow within horizontal rectangular channels with small heights. Int. J. Multiph. Flow, 27, 783–796. DOI: 10.1016/S0301-9322(00)00050-1.
  • 13. Lockhart R., Martinelli R., 1949. Proposed correlations of data for isothermal two-phase, two-component flow in pipes. Chem. Eng. Progr., 45, 39-48.
  • 14. Mishima K., Hibiki T., 1996. Some characteristics of air–water two-phase flow in small diameter vertical tubes. Int. J. Multiph. Flow, 22, 703–712. DOI: 10.1016/0301-9322(96)00010-9.
  • 15. Owens W.L., 1961. Two-phase pressure gradient. Int. Development in Heat Transfer, Pt II. ASME, New York.
  • 16. Saisorn S., Wongwises S., 2010. The effects of channel diameter on flow pattern, void fraction and pressure drop of two-phase air-water flow in circular micro-channels. Exp. Therm. Fluid. Sci., 34, 454-462. DOI: 10.1016/j.expthermflusci.2009.02.006.
  • 17. Yue J., Chen G., Yuan Q., 2004. Pressure drops of single and two-phase flows through T-type microchannel mixers. Chem. Eng. J., 102, 11-24. DOI: 10.1016/j.cej.2004.02.001.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BPK6-0026-0005
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