1 McFarlane, R.C., Muller, T.D., Miller, F.G., “Unsteady-state distribution of fluid composition in two-phase oil reservoirs undergoing gas injection”, Soc. Petrol. Eng. J., 7 (1), 61-74 (1967). 2 We, C., Farouqali, S.M., Stahl, C.D., “Experimental and numerical simulation of two-phase flow with interface mass transfer in one and two dimensions”, Soc. Petrol. Eng. J., 9 (3), 323-337 (1969). 3 Wang, X.L., Liu, C.J., Yuan, X.G., Yu, K.T., “Computational fluid dynamics simulation of three-dimensional liquid flow and mass transfer on distillation column trays”, Ind. Eng. Chem. Res., 43, 2556-2567 (2004). 4 Liu, B.T., “Study of a new mass transfer model of CFD and its application on distillation tray”, Ph.D. Thesis, Tianjin University, Tianjin, China (2003). (in Chinese) 5 Sun, Z.M., Liu, B.T., Yuan, X.G., Yu, K.T., “New turbulent model for computational mass transfer and its application to a commercial-scale distillation column”, Ind. Eng. Chem. Res., 44 (12), 4427-4434 (2005). 6 Bird, R.B., Steward, W.E., Lightfoot, E.N., Transport Phenomena, 2nd ed., John Wiley & Sons (2002). 7 Rosén, C., Trägårdh, C., “Prediction of turbulent high Schmidt number mass transfer using a low Reynolds number k-ε turbulent model”, Chem. Eng. J., 59, 153-159 (1995). 8 Sun, Z.M., Yu, K.T., Yuan, X.G., Liu, C.J., “A modified model of computational mass transfer for distillation column”, Chem. Eng. Sci., 62, 1839-1850 (2007). 9 Liu, G.B., Yu, K.T., Yuan, X.G., Liu, C.J., Guo, Q.C., “Simulations of chemical absorption in pilot-scale and industrial-scale packed columns by computational mass transfer”, Chem. Eng. Sci., 61, 6511-6529 (2006). 10 Liu, G.B., Yu, K.T., Yuan, X.G., Liu, C.J., “New model for turbulent mass transfer and its application to the simulations of a pilot-scale randomly packed column for CO2-NaOH chemical absorption”, Ind. Eng. Chem. Res., 45, 3220-3229 (2006). 11 Bachmat, Y., Bear, J., “Macroscopic modelling of transport phenomena in porous media (1) The continuum approach”, Transport Porous Media, 1 (3), 213-240 (1986). 12 Liu, G.B., Yu, K.T., Yuan, X.G., Liu, C.J., “A computational transport model for wall-cooled catalytic reactor”, Ind. Eng. Chem. Res., 47, 2656-2665 (2008). 13 Sakata, M., Yanagi, T., “Performance of a commercial scale sieve tray”, In: Institution of Chemical Engineers Symposium Series, 3.2, American Institute of Chemical Engineers, New York, 21-34 (1979). 14 Liu, G.B., “Computational transport and its application to mass transfer and reaction processes in packed-bed”, Ph.D. Thesis, Tianjin University, Tianjin, China (2006). (in Chinese) 15 Shariat, A., Kunesh, J.G., “Packing efficiency testing on a commercial scale with good (and not so good) reflux distribution”, Ind. Eng. Chem. Res., 34 (4), 1273-1279 (1995). 16 Valstar, J.M., van den Berg, P.J., Oyserman, J., “Comparison between two dimensional fixed bed reactor calculations and measurements”, Chem. Eng. Sci., 30 (7), 723-728 (1975). 17 Sun, Z.F., Yu., K.T., Wang, S.Y., Miao, Y.Z., “Absorption and desorption of carbon dioxide into and from organic solvents: Effects of Rayleigh and Marangoni instability”, Ind. Eng. Chem. Res., 41, 1905-1913 (2002). 18 Sha, Y., Cheng, H., Yuan, X.G., Yu, K.T., “Kinetics of mass transfer accompanied by Marangoni effect”, J. Chem. Ind. Eng. (China), 54 (11), 1518-1523 (2003). (in Chinese) 19 Sha, Y., Yuan, X.G., Cheng, H., Yu, K.T., “Rayleigh-Bénard-Marangoni effect in mass transfer”, Chemical Engineering (China), 31 (5), 8-13 (2003). (in Chinese) 20 Yu, L.M., Zeng, A.W., Yu, K.T., “Effect of interfacial velocity fluctuations on the enhancement of the mass-transfer process in falling-film flow”, Ind. Eng. Chem. Res., 45, 1201-1210 (2006). |