[1] Y. Haroun., L. Raynal,” Use of Computational Fluid Dynamics for Absorption Packed Column Design”, Oil and Gas Science and Technology– Rev. IFP Energies nouvelles, 71, 43, (2016).
[2] Liu, Q.S., Roux, B., Velarde, M.G., “Thermocapillary Convection in Two-Layer Systems”, International Journal of Heat and Mass Transfer, 41(11), 1499(1998).
[3] Ludwig, Applied Process Design for Chemical and Petrochemical Plants, 3rd ed., 2, Gulf Professional Publishing, 230(1979).
[4] Leva, M., Weintraub, M., Grummer, M., Pollchik, M., & Storch, H. H. Fluid Flow through packed and Fluidized systems. United States, Bureau of Mines, Bulletin 504 (1951).
[5] E. Ozahi, Gundogdu, M.Y., Carpinlioglu, M.O., “A Modification on Ergun’s Correlation for Use in Cylindrical Packed Beds With Non-spherical Particles”,Advanced Powder Technology,19,369(2008).
[6] Wu, J., Yu, B., Yun, M., “A resistance model for flow through porous media” Transp Porous Med,71, 331(2008).
[7] S. Ergun, Fluid flow through packed columns, Chem. Eng. Prog. 48, 89(1952).
[8] Cohen, Y., Metzener, A. B.,”Wall Effects in Laminar Flow of Fluids through Pocked Beds”, AlChEJ., 27(5), 705 (1981).
[9] Foumeny, E. A., Benyahia, F., Castro, J. A. A., Moallemi, H. A., Roshani, S., “Correlations of pressure drop in packed beds taking into account the effect of confining wall”, International Journal of Heat and Mass Transfer, 36(2), 536 (1993).
[10] W. Reichelt, Zur Berechnung des Druckverlustes einphasig durchströmter Kugel- und Zylinderschüttungen, Chem. Ing. Tech., 44, 1068 (1972).
[11] Eisfeld. B., Schnitzlein. K., “The influence of confining walls on the pressure drop in packed beds”, Chem. Eng. Sci., 56, 4321 (2001).
[12] Atmakidis, T., Y. Kenig, E., “CFD-based analysis of the wall effect on the pressure drop in packed beds with moderate tube/particle diameter ratios in the laminar flow regime”, Chem. Eng. J., 155, 404(2009).
[13] D. Sebastia-Saez et al.” Meso-scale CFD study of the pressure drop, liquid hold-up, interfacialarea and mass transfer in structured packing materials”, International Journal of Greenhouse Gas Control, 42,399 (2015).
[14] Caulkin,R., Jia, X., Fairweather, M., Williams, R.A., “Predictions of Porosity and Fluid Distribution through Nonspherical-Packed Columns”, AIChEJ., 58(5), 1503 (2012).
[15] Boyer, C., Koudil, A., “Study of liquid spreading from a point source in a trickle bed via gamma-ray tomogeraphy and CFD simulation”, Chem. Eng. Sci., 60, 6279(2005).
[16] Liu, S., Long, J.,” Gas–liquid countercurrent through packed towers”, Journal of Porous Media, 2(2), 99(2000).
[17] de Klerk, A.,” Voidage Variation in Packed Beds at Small Column to Particle Diameter Ratio”, AIChEJ, 49(8), 2022(2003).
[18] Sun C. G., Yin. F. H., Afcan. A., Nandakumar. K., and Chuang. K. T., “Modeling and Simulation of Flow maldistribution in random packed columns with gas-liquid countercurrent flow”, Trans. IChemE., 78(Part A), 378 (2000).
[19] Yin F. H., Sun C. G., Afacan A., Nandakumar K., Chuang K. T.,” CFD Modeling of Mass-Transfer Processes in Randomly Packed Distillation Columns,” Ind. Eng. Chem. Res., 39, 1369(2000).
[20] Jiang Y., Khadilkar Mohan R., Al-Dahhan Muthanna H., Dudukovi Milorad P.,” CFD modeling of multiphase flow distribution in catalytic packed bed reactors: scale down issue”, Catalysis Today, 66, 209(2001).
[21] 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(2006).
[22] Liu,G,B .,Yu ,K.T., “A numerical method for predicting the performance of a randomly packed distillation column” , International Journal of Heat and Mass Transfer, 52 ,5330(2009).
[23] Fourati, M., Roig, V., Raynal, L.,”Liquid dispersion in packed columns: Experiments and Numerical modeling”, Chem. Eng. Sci. (2013).
[24] Geankoplis, Christie J. Transport Process and Unit Operations.3rd ed.
Prentice Hall: New Jersey, chapter 3 (2003).
[25] Iliuta I., Larachi F., “Three-dimensional simulation of gas-liquid concurrent down flow in vertical, inclined, and oscillating packed beds, AIChEJ, 62(3), p.916(2016).