[1] Xu Ch., Zhu J.X., Effects of Gas Type and Temperature on the Particle Fluidization, Particuology, 4, p. 114 (2006).
[2] Formisian B., Girimonte R., Mancuso L., Analysis of the Fluidization Process of Particle Beds at High Temperature, Chem. Eng. Sci., 53, p. 951 (1997).
[3] Formisiani B., Girimonte R., Pataro G., The Influene of Operating Temperature on the Dense Phase Properties of Bubbling Fluidized Beds of Solids, Powder Technology, 125, p. 28 (2002).
[4] Guo O., Yue G., Suda T., Sato J., Flow Characteristics in a Bubbling Fluidized Bed at Elevated Temperature, Chemical Engineering and Processing, 42, p. 439 (2003).
[5] J.Subramani H., Balaiyya M.B.M., Miranda L.R., Minimum Fluidization Velocity at Elevated Temperature for Geldart's Group-B Powders, Experimental Thermal Fluid Science, 32, p. 166 (2007).
[6] Geldart D., Kapoor D.S., Bubble Sizes in a Fluidized Bed at Elevated Temperatures, Chem. Eng. Sci., 31, p. 842 (1976).
[7] Kai, T., Furusaki, S., Behavior of Fluidized Beds of Small Particles at Elevated Temperatures, J. Chem. Eng. Japan, 18, p. 113 (1985).
[8] Hatate Y., Ohmagari K., Ikari A., Kondo K., King D.F., Behavior of Bubbles in Cylindrical Fluidized Bed at an Elevated Temperature, J. Chem. Eng. Japan., 21, p. 424 (1988).
[9] Kunii D., Levenspiel O., “Fluidization Engineering”, Butterworth-Heinemann, New York, Second Edition, (1991).
[10] Lettieri P., Newton D., Yates J.G., The Influence of Interparticle Forces on Fluidization Behavior of Some Industrial Materials at High Temperature, Powder Technology, 110, p. 117 (2000).
[11] Lettieri P., Newton D., Yates J.G., High Temperature Effects on the Dense Phase Properties of Gas Fluidized Beds, Powder Technology, 120, p. 34 (2001).
[12] Cui H., Sauriol P., Chaouki J., High Temperature Fluidized Bed Reactor: Measurements, Hydrodynamics and Simulation, Chem. Eng. Sci., 58, p. 3413 (2003).
[13] Cui H., Chaouki J., Effects of Temperature on Local Two-Phase Flow Structure in Bubbling and Turbulent Fluidized Beds of FCC Particles, Chem. Eng. Sci., 59, p. 3413 (2004).
[14] Radmanesh R., Mabrouk R., Chaouki J., Guy C., The Effect of Temperature on Solids Mixing in a Bubbling Fluidized Bed Reactor, Inter. J. Chem. Reactor Eng., 3, A16, (2004).
[15] Larachi F., Chaouki J., Kennedy G., 3-D mapping of Solids Flow Fields in Multiphase Reactor with RPT, AIChE J., 41, p. 439 (1995).
[16] Mostoufi N., Chaouki J., Local Solid Mixing in Gas-Solid Fluidized Beds, Powder Technology., 14, p. 23 (2001).
[17] Mostoufi N., Chaouki J., On the Axial Movement of Solids in Gas-Solid Fluidized Beds Source: Chem. Eng. Res. & Des. Part A Transactions of the Institute of Chemical Engineers., 78, p. 911 (2000).
[18] Stein M., Ding Y.L., Seville J.P.K., Parker D.J., Solids Motion in Bubbling Gas Fluidized Beds, Chem. Eng. Sci., 55, p. 5291 (2000).
[19] Mostoufi N., Chaouki J., Flow Structure of the solids in Gas-Fluidized Beds, Chem. Eng. Sci., 59, p. 4217 (2004).
[20] Mabrouk R., Chaouki J., Guy C., Effective Drag Coefficient Investigation in the Acceleration Zone of an Upward Gas-Solid Flow, Chem. Eng. Sci., 62, p. 318 (2007).
[21] Bai D., Jin Y., Z.Q., Acceleration of Particles and Momentum Exchange Between Gas and Solids in Fast Fluidized Beds, in: M. Kwauk, M. Hasatani (Eds.) "Fluidization VI, Science and Technology", Science Press, Beijing, 46-55, (1991).
[22] Gidaspow, D., "Multiphase Flow and Fluidization, Continuum and Kinetic Theory Description", Academic Press, San Diego, CA, (1994).
[23] Cui H., Mostoufi N., Chaouki J., Characterization of Dynamic Gas-Solid Distribution in Fluidized Beds, Chem. Eng. J., 79, p. 133 (2000).