T he method for drying suspensions and solutions in a bed of inert particles of spoutable size, was first developed at the former Leningrad Institute of Technology for applications where the dried solids were ultimately required in the form of a fine powder (Reger et al., 1967;Romankov and Rashkovskaya, 1968;Minchev et al., 1969a, b). Since then, this technique has been used for drying chemicals (Mathur and Epstein, 1974;Ormos and Blickle, 1980) as well as biological products such as: animal blood, animal blood plasma, egg white, and protein-containing solutions, among others (Fane et al., 1980;Pham and Pooley, 1981;Pham, 1983;Rashkovskaya et al., 1979;Kutsakova and Utkin, 1983). More recently, reports by Markowski (1992), Reyes et al. (1998), Brereton and Lim (1993), Ochoa-Martínez et al. (1993), Szentmarjay et al. (1996) and Tia et al. (1995) who dried a variety of products, ranging from chemicals to liquid foods, have shown the feasibility of the process to obtain good quality dry powdered solids, which make the system, a low-cost, compact alternative to spray drying. Most of these authors have worked with conventional spouted beds, and practically none of them mention any limitations to the system employed.On this topic, Osorio (1990) and Ochoa-Martínez et al. (1993) reported that in spite of the great superficial area present in the bed of inert particles in a conventional spouted bed dryer, only a small fraction of this is really used during the drying process (2% to 10% of the total area, depending on the operating conditions). The effective area, increased slightly with the spouting velocity, but nevertheless this fraction remained small in contrast to the available area. These authors also reported that the maximum bed wet fraction that can be utilized in the drying process for a given inlet temperature, spouting velocity and feed conditions, is limited by the stability of the fountain. If the wet fraction of the bed exceeds a certain value, fixed by operations conditions, the spouting becomes unstable.On the other hand, the amount of heat that the annular region of the bed can provide for the evaporation of moisture, is practically unaffected by the spouting velocity. As the spouting velocity increases, a larger pro-