[1] Tomotika S., On the Instability of a Cylindrical Thread of a Viscous Liquid Surrounded by Another Viscous Fluid, “Proceedings of Royal Society of London” 150A, p. 322 (1935).
[2] Rayleigh J.W.S., On the Instability of Jets, “Proceedings of the LondonMathematical Society”, 10, p. 4 (1879).
[3] Meister B.J., Scheele G.F., Drop Formation from Cylindrical Jets in Immiscible Liquid Systems, AIChE J., 15, p. 700 (1969).
[4] Scheele G.F., Meister B.J., Drop Formation at Low Velocities in Liquid-Liquid Systems:part 1.Prediction of Drop Volume, AIChE J.,14, p. 9 (1968a).
[5] Scheele G.F., Meister B.J., Drop Formation at Low Velocities in Liquid-Liquid Systems: Part 2. Prediction of Jetting Velocity, AIChE J.,14, p. 15 (1968b).
[6] Christiansen R.M., Hixson A.N., Breakup of a liquid jet in a denser liquid, Ind. Eng. Chem., 49, p. 1017 (1957).
[7] Kitamura Y., Mishima H., Takahashi T., Stability of Jets in Liquid-Liquid Systems ,Canadian Journal of Chemical Engineering.,60, p. 723(1982).
[8] Bright A., Minimum Drop Volume in Liquid Jet breakup,Chem.Eng.Res.,63, p. 59 (1985) .
[9] Tyler E., Instability of Liquid Jets, Philos .Mag., 16, p.504 (1933).
[10] Richards J.R., Beris A.N., Lenhoff, A.M., Steady Laminar Flow of Liquid-Liquid Jets at High Reynolds Numbers, Phys. Fluids., 5 A, 1703 (1993).
[11] Richards J.R., Beris A.N., Lenhoff A.M., Dynamics Breakup of Liquid-Liquid Jets, Phys. Fluids., 6, p. 2640 (1994).
[12] Richards J.R., Beris A.N., Lenhoff A.M., Drop Formation in Liquid-Liquid Systems Before and After jetting, Phys. Fluids., 7, p. 2617 (1995).
[13] Homma S., Koga J., Matsumoto S., Song M. and Tryggvason G., Breakup Mode of an Axisymmetric Liquid Jet Injected into Another Immiscible Liquid, Chem. Eng. Sci., 61, p. 3986 (2006).
[14] Richards J.R., Scheele G.F., Measurement of Laminar Jet Velocity Distributions in Liquid-Liquid Systems Using Flash Photolysis, Chem. Eng. Commun. , 36, p. 73 (1987).
[15] Yu H., Scheele G.F., Laminar Jet Contraction and Velocity Distribution in Immiscible Liquid-Liquid Systems, Int .J. Multiphase Flow., 2, p. 153 (1975).
[16] Gospodinov P., Radev S., PenchevI., Velocity Profiles and Form of a Laminar Jet in Immiscible Liquid-Liquid Systems, Int. J .multiphase Flow .,5, p. 87 (1979).
[17] Garner F.H., Mina P., Jenson V.G., Velocity Distribution Inside Liquid-Liquid Jets, Trans. Faraday Soc., 55, 1627 (1959).
[18] Meister B.J., Scheele G.F., Prediction of jet length in Immiscible Liquid Systems, AIChE J., 15, p. 689 (1969b).
[19] Sawistowski H., Influence of Mass Transfer Induced Marangoni Effects on Magnitude of Interfacial Area and Equipment Performance in Mass Transfer Operations,Chem.Ing.Tech.,45, p. 1114(1973) .
[20] Burkholder H.C., Berg J.C., Effect of Mass Transfer on Laminar Jet Breakup, AIChE J., 20 , p. 863 (1974).
[21] Burkholder H.C., Berg J.C., Effect of Mass ransfer on Laminar Jet Breakup, AIChE J., 20, p. 872 (1974).
[22] Skelland A.H.P., Huang Y.F., Dispersed Phase Mass Transfer During Drop Formation under Jetting Conditions, AIChE J., 23, p. 701 (1977).
[23] Coyle R.W., Berg J.C., Niwa, J.C., Instability of Liquid Jets, Chem. Eng. Sci., 36, p. 19 (1981).
[24] Kimura S., Miyauchi T., Mass Transfer in a Liquid-Liquid Laminar Jet, Chem. Eng. Sci., 21, p. 1057 (1966).
[25] Garde R.J., “Turbulent flow”, JohnWiley&Sons,New York, (1994) .
[26] Bernard P.S., Wallace, J.M., “Turbulent flow”, Wiley,New York, (2002).
[27] Godfrey J.C., Slater M.J., “Liquid-Liquid Extraction Equipment”, John Wiley & Sons,New York, (1994).
[28] Misek T.," Recommended Systems for Liquid Extraction Studie"s, Pub. Instn. Chem. Engs. For EFCE (1978).
[29] Ghalechian J.S., Slater M.J., A Possible Approach to Improving Rotating Disc Contactor Design Accounting for Drop Breakage and Mass Transfer with Contamination, Chem. Eng.J., 75, p. 131(1999).
[30] Chen C.J., Nikitopoulos P., On the Near Field Characterization of Axisymmetric Turbulent Buoyant Jets in a Uniform Environment, J. Heat Transfer., 22, p. 245 (1979).
[31] Molaei Dehkordi A., Application of a Novel-Opposed-Jets Contacting Device in Liquid-Liquid Extraction, Chem. Eng. Sci., 41, p. 251(2001).
[32] Asai S., Hatanaka J., Maeda H., Mass Transfer in a Liquid-Liquid Jet with Cocurrent Laminar Flow, Chem. Eng. Sci., 43, p. 713 (1988).
[33] Saien J., Zonouzian A., Molaei Dehkordi A., Investigation of a Two Impinging-Jets Contacting Device for Liquid-Liquid Extraction Processes, Chem. Eng. Sci.,61, 942 (2006) .
[34] Yang C., Mao Z.S., Numerical Simulation of Interphase Mass Transfer with the Level Set Approach, Chem. Eng. Sci., 60, 2643 (2005).
[35] Evans G.M., Machniewski P.M., Mass Transfer in a Confined Plunging Liquid Jet Bubble Column, Chem. Eng. Sci., 54, 4981 (1999).
[36] Jamshidi A.M., Sohrabi M., Hydrodynamics and Mass Transfer Characterization of a Down Flow Jet Loop Bioreactor, Bio. Eng. J., 8, 241 (2001).
[37] Demuren A.O., Multigrid Acceleration and Turbulence Models for Computations of 3D Turbulent Jets in Crossflow, J. Heat Transfer., 35, p. 2783 (1992).
[38] Treybal R.E., “Mass Transfer Operations”, 3rd Ed.,Mc Graw-Hill,New York, (1990).
[39] Mc Cabe W.L., Smith J.C., “Unit Operation of Chemical Engineering”, 6th Ed., McGraw- Hill,New York, (2001).