The authors have studied pulverization of limestone by the Tower Mill to develop more valuable uses of this resources. In the process of this study, the Tower Mill KD-3, a modified version of the Tower Mill KD-2, was used as equipment. As for the KD-2, this type is composed of three parts: comminuting, classifying and collecting part. But in the KD-3 classified coarse particles are settled in the bottom of the classifying part for another products. It is worth noticing that the air flow through the nets set improved classification of ground particles. In each experiment, to investigate the factors affecting the weight and the particles size of pulverized products, the weights of steel balls, limestone and the number of revolutions of screw were kept constant, while the grinding part and the air flow rate (Um) in the classifying part were varied.The results obtained are summarized as follows: 1) The fine particles classified in the classifying part flow into the cyclone smoothly with the air while the coarse particles are settled in the bottom of the classifying part for another products because of the modified structure of this classifying part and the set nets.2) The weight of products were affected by the dead space in the comminuting part, the inlet surface area and the number of spirals in the cyclone.3) The ratio of secondary particles influenced the weight of the-10μm particles and the 50% particles diameters in the product.4) The maximum values of the particle diameter (Dmax) in the product collected by the cyclone were found to be in accordance with the Stokes's law.5) The decrease and uniformity of the flow rate made the Dmax values smaller.6) The minimum value of Dmax was: 8.2μm for products collected by the cyclone; 14.7μm for another products settled in the bottom of classifying part.