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10 6 10 5 0 5 10 15 Normalized Average SNR of First Path [dB]

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Heat conduction in the liquid film and in the apparatus wall is also not considered. Any non-conversed reactant of the suspension and the reaction product are deposited on fluidized-bed material after the drying process, and can be removed from the bed material by attrition. The dust due to the attrition is elutriated with the gas flow from the fluidized bed. The hold-up material and the sprayed solid with the suspension have same densities. Agglomeration and breakage processes are not considered. The granulation process follows the surface-proportional growth. The attrition process is described with a surface-proportional attrition coefficient. There is no particle discharge due to hydrodynamic processes. The residence time of the dust feeding from outside of the granulator is negligibly small. The Reynolds number at the fluidizing point is computed according to Goroschko [26]. The computation of the relative void volume is also calculated according to Goroschko [26]. The heat and mass transfer coefficients between gas and particle are computed according to Gnielinski [25]. The computation of the heat losses from the apparatus wall to the environment is done with the equations proposed by Kast and Klan [48]. The steam pressure of the water vapor in the model is determined by the method of Baehr [4]. The description of the surface proportional growth of granulates follows according to M rl [67, 68]. The description of the surface proportional attrition of granulates is taken from Rangelova [75].

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