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Semi-Empirical Analysis of the Mass Transfer Characteristics of the Slug Flow in Vertical Mesoscale Tubes

작은 수직관을 흐르는 슬러그 유동의 물질전달 특성에 대한 반경험적 해석

  • Kim, Dong-Seon (Department of Mechanical Engineering, Korea National University of Transportation)
  • 김동선 (한국교통대학교 기계공학과)
  • Received : 2013.08.23
  • Accepted : 2014.05.20
  • Published : 2014.08.10

Abstract

Experimental mass transfer data, which were obtained for the $CO_2$-water slug flows in vertical tubes with 2, 5, and 8mm diameters, were analyzed in comparison with the penetration theory. It was found that a penetration model with molecular diffusion coefficient cannot predict the experimental data accurately. An effective diffusion coefficient, which considers enhancement effect of interfacial waves, was suggested to improve prediction. Another empirical factor was also suggested to consider the effect of non-uniform interface velocity. A modified penetration model was found to be capable of predicting the experimental data reasonably well.

Keywords

References

  1. Cheng, L. and Mewes, D., 2006, Review of two-phase flow and flow boiling of mixtures in small and mini channels, International Journal of Multiphase Flow, Vol. 32, No. 2, pp. 183-207. https://doi.org/10.1016/j.ijmultiphaseflow.2005.10.001
  2. Ribatski, G., Wojtan, L., and Thome, J. R., 2006, An analysis of experimental data and prediction methods for two-phase frictional pressure drop and flow boiling heat transfer in micro-scale channels, Experimental Thermal and Fluid Science, Vol. 31, No. 1, pp. 1-19. https://doi.org/10.1016/j.expthermflusci.2006.01.006
  3. Lee, K. J. and Kim, D. S., 2012, Mass transfer characteristics of the carbon dioxide-water slug flow in vertical small-bore tubes, Korean Journal of Air Conditioning and Refrigeration Engineering, Vol. 24, No. 5, pp. 401-408. https://doi.org/10.6110/KJACR.2012.24.5.401
  4. Kye, S. H. and Kim, D. S., 2013, Flow characteristics of a gas-liquid slug flow in small vertical tubes, Korean Journal of Air Conditioning and Refrigeration Engineering, Vol. 25, No. 5, pp. 246-254. https://doi.org/10.6110/KJACR.2013.25.5.246
  5. Higbie, R., 1935, The rate of absorption of a pure gas into a still liquid during short periods of exposure, Transactions American Institute of Chemical Engineers, New York, Vol. 31, No. 2, pp. 368-389.
  6. Lamourelle, A. P. and Sandall, O. C., 1972, Gas absorption into a turbulent liquid, Chemical Engineering Science, Vol. 27, No. 5, pp. 1035-1043. https://doi.org/10.1016/0009-2509(72)80018-6
  7. Tomida, T. and Yoshida, M., 1976, Liquid-side volumetric mass transfer coefficient in upward two-phase flow of air-liquid mixtures, Journal of Chemical Engineering of Japan, Vol. 9, No. 6, pp. 464-468. https://doi.org/10.1252/jcej.9.464
  8. van Baten, J. M. and Krishna, R., 2004, CFD simulations of mass transfer from Taylor bubbles rising in circular capillaries, Chemical Engineering Science, Vol. 59, No. 12, pp. 2535-2545. https://doi.org/10.1016/j.ces.2004.03.010
  9. Vandu, C. O., Liu, H., and Krishna, R., 2005, Mass transfer from Taylor bubbles rising in single capillaries, Chemical Engineering Science, Vol. 60, No. 22, pp. 6430-6437. https://doi.org/10.1016/j.ces.2005.01.037
  10. Johnstone, H. F. and Pigford, R. L., 1942, Distillation in a wetted-wall column, Transactions American Institute of Chemical Engineers, New York, Vol. 38, pp. 25-50.
  11. Brauer, H., 1971, Stoffaustausch, Verlag Sauerlander, Aarau.
  12. Welty, J., Wicks, C. E., Wilson, R. E., and Rorrer, G. L., 2007, Fundamentals of momentum, heat and mass transfer, 5th Ed., Wiley.
  13. Kashid, M. N., Renken, A., and Kiwi-Minsker, L., 2011, Gas-liquid and liquid-liquid mass transfer in microstructured reactors, Chemical Engineering Science, Vol. 66, No. 17, pp. 3876-3897. https://doi.org/10.1016/j.ces.2011.05.015
  14. Yoshimura, P. N., Nosoko, T., and Nagata, T., 1996, Enhancement of mass transfer into a falling laminar liquid film by two-dimensional surface waves-Some experimental observations and modeling, Chemical Engineering Science, Vol. 51, No. 8, pp. 1231-1240. https://doi.org/10.1016/0009-2509(95)00387-8
  15. Yih, S. M. and Chen, K. Y., 1982, Gas absorption into wavy and turbulent falling films in a wetted wall column, Chemical Engineering Communications, Vol. 17, No. 1-6, pp. 123-136. https://doi.org/10.1080/00986448208911620
  16. Vivian, J. E. and Peaceman, D. W., 1956, Liquid-side resistance in gas absorption, AIChE Journal, Vol. 2, No. 4, pp. 437-443. https://doi.org/10.1002/aic.690020404
  17. Irandoust, S., Ertle, S., and Andersson, B., 1992, Gas-liquid mass transfer in Taylor flow through a capillary, The Canadian Journal of Chemical Engineering, Vol. 70, No. 1, pp. 115-119. https://doi.org/10.1002/cjce.5450700116
  18. Roudet, M., Loubiere, K., Gourdon, C., and Cabassud, M., 2011, Hydrodynamic and mass transfer in inertial gas-liquid flow regimes through straight and meandering millimetric square channels, Chemical Engineering Science, Vol. 66, No. 13, pp. 2974-2990. https://doi.org/10.1016/j.ces.2011.03.045
  19. Esteves, M. T. S. and De Carvalho, J. R. F. G., 1993, Liquid-side mass transfer coefficient for gas slugs rising in liquids, Chemical Engineering Science, Vol. 48. No. 20, pp. 3497-3506. https://doi.org/10.1016/0009-2509(93)85005-A
  20. Brown, R. A. S., 1965, The mechanics of large gas bubbles in tubes : I. Bubble velocities in stagnant liquids, The Canadian Journal of Chemical Engineering, Vol. 43, No. 5, pp. 217-223. https://doi.org/10.1002/cjce.5450430501

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