[1] Taylor R., Krishna R., "Multicomponent Mass Transfer", Wiley-Interscience, (1993).
[2] Zhao D., Guo L., Lin C., Zhang X., An Experimental Study on Local Interfacial Area Concentration Using a Double-Sensor Probe. Int J Heat Mass Transf., 48, p. 1926 (2005).
[3] Pohorecki R., Moniuk W., Bielski P., Sobieszuk P., Da. Browiecki G., Bubble Diameter Correlation via Numerical Experiment. Chem Eng J., 113, p. 35 (2005).
[4] Delhaye J.M., Brichard P., Interfacial Area in Bubbly Flow: Experimental Data and Correlation. Nucl Eng Des., 151, p. 65 (1994).
[5] Tomida T., Yusa F., Akazaki T., Effective Interfacial are and Liquid Side Mass Transfer Coefficient in Upward Two-Phase Flow of Gas-Liquid Mixtures. Chem Eng J., 16, p. 81 (1978).
[6] Martin R., Wagner H., Po¨pel J., Kalte P., Pure Oxygen Desorption Method- a New and Cost-Efective Method for the Determination of Oxygen Transfer Rates in Clean Water. Wat Sci Tech., 38, p. 103 (1998).
[7] Puskeiler R., Weuster-Botz D., Combined Sulfite Method for the Measurement of the Oxygen Transfer Coefficient kLa in Bioreactors. J Biotechnol., 120,430–438 (2005).
[8] Van Baten J.M., Krishna R., Modeling Sieve Tray Hydraulics Using Computational Fluid Dynamics, Chem. Eng. J., 77, p. 143 (2000).
[9] Krishna R., van Baten J.M., Ellenberger J., Higler A.P., Taylor R., CFD Simulations of Sieve Tray Hydrodynamics, Chem. Eng. Res. Des., Trans. Inst. Chem. Eng., 77, p. 639 (1999).
[10] رهبر رحیمی، محمودرضا رحیمی، فرهاد شهرکی، بررسی توانمندی دینامیک سیالات محاسباتی در طراحی سینی های غربالی، نشریه شیمی و مهندسی شیمی ایران، 24و19 (1384).
[11] محمودرضا رحیمی، "شبیه سازی هیدرودینامیک، انتقال حرارت و انتقال جرم در سینی های غربالی برج تقطیر با استفاده از دینامیک سیالات محاسباتی"، پایان نامه دکتری مهندسی شیمی، دانشگاه سیستان و بلوچستان (1385).
[12] Gesit G.K., Nandakumar K., Chuang K.T., CFD Modeling of Flow Patterns and Hydraulics of Commercial-Scale Sieve Trays, AIChE. J., 49, p. 910 (2003).
[13] Rahimi R., Rahimi M.R., Shahraki F., Zivdar M., Efficiencies of Sieve Tray Distillation Columns by CFD Simulations, Chem. Eng. Technol.J., 29(3), p. 326 (2006).
[14] Rahimi M.R., Karimi H., A 3-D Two-Fluid CFD Model for Hydrodynamics of Industrial Scale Sieve Trays with Nonuniform Gas Distribution, "11th International Conference on Multiphase Flow in Industrial Plants", Palermo, Italy, 7-10 sept. (2008).
[15] Rahimi M.R., Karimi H., CFD Simulation of Hydraulics of Sieve Trays with Gas Mal-Distribution, Chemical Product and Process Modeling , 5(1), Article 2 (2010).
[16] Alizadehdakhel A., Rahimi M., Abdulaziz Alsairafi A., Numerical and Experimental Investigation on a New Modified Valve in a Valve Tray Column, Korean Journal of ChemicalEngineering, 26(2), p. 475 (2009).
[17] Zarei T., Rahimi R., Zivdar M., Computational Fluid Dynamic Simulation of MVG Tray Hydraulics, Korean Journal of Chemical Engineering, 26(5), p. 1213 (2009).
[18] Li X.G., Liu D.X., Xu S.M. Li H., CFD Simulation of Hydrodynamics of Valve Tray, Chemical Engineering & Processing: Process Intensification, 48(1), p. 145 (2009).
[19] Rahimi M.R., Rahimi R., Shahraki F., Zivdar M., Prediction of Temperature and Concentration Distributions of Distillation Sieve Trays by CFD, Tamkang Journal of Science and Engineering, 9(3), p.265 (2006).
[20] Krishna R., Urseanu M.I., van Baten J.M., Ellenberger J., Rise Velocity of a Swarm of Large Gas Bubbles in Liquids, Chem. Eng. Sci., 54, 171 (1999).
[21] Bennett D.L., Agrawal B., Cook P.J., New Pressure Drop Correlation for Sieve Tray Distillation Column, AIChE J., 29, p. 434 (1983).
[22] Solari R.B., Bell R.L., Fluid Flow Patterns and Velocity Distribution on Commercial-Scale Sieve Trays, AIChE J., 32, p. 640 (1986).
[23] Olujic Z., Jodecke M., Shilkin A., Schuch G., Kaibel B., Equipment Improvement Trends in Distillation, Chem. Eng. Process., 48, p. 1089 (2009).
[24] Brambilla A., The Effect of Vapor Mixing on Efficiency of Large-Diameter Distillation Plates, Chem. Eng. Sci., 31, p. 571 (1976).
[25] Zuiderweg F.J., Sieve Trays: A View on the State of the Art, Chem. Eng. Sci., 37, p. 1441 (1982).