“…This limitation is even more obvious when wet and sticky materials are treated in the fluidization units: in this situation, a separate control of gas flows to the spout (mainly acting as a mixing means, besides promoting effective mass transfer, though for a very short time) and to the annulus (where equilibrium between the moving phases can be easily reached, thus stopping the phenomenon) is desirable (Hattori et al, 2001). The addition of a draft tube (Arsenijevic et al, 2004;Hattori et al, 2001;Ijichi, Miyauchi, Uemura, & Hatate, 1998;Ishikura, Nagashima, & Ide, 2003;Ji, Tsutsumi, & Yoshida, 1997Khoe & Van Brakel, 1983;Muir, Berruti, & Behie, 1990;Osorio Revilla et al, 2004a;Osorio Revilla et al, 2004b;Stocker et al, 1989) has proven to act as a beneficial constraint and helps in terms of a better definition of both the gas distribution and the solids motion pattern during various processes such as drying (Khoe & Van Brakel, 1983;Tulasidas et al, 1993), coal gasification, combustion (Konduri et al, 1995, Konduri, Altwicker, & Morgan, 1999 pyrolysis of hydrocarbons (Stocker et al, 1989) and production of pharmaceuticals (Fukumori & Ichikawa, 1997;Littman, Morgan, & Morgan, 1997). A paste-like agglomerate surely benefits from such a geometrical configuration which assures the intermixing of the solids and close contact with the drying fluid medium.…”