This article analyzes the movement of particles of different components in the inter-row space and in the peripheral part of the disintegrator's working chamber. The diagram of the disintegrator with the component loading unit and the diagram of the disintegrator's working chamber are presented. The loading unit consists of two screw feeders, which supply various components to the conical loading hopper. The capacity of the screw feeders is matched with the capacity of the hopper and the vertical cylindrical branch pipe. The mass capacity of the mixing chamber and the grinding of the disintegrator is determined. Mass throughput is determined using the functional dependence of the change in the bulk density of the material during its passage in the radial direction from the radius of scattering disk Rд to the radial size of the disintegrator body. It is determined that the mass throughput depends on the geometric (Rk, Rg, H) and technological (ϑ_r ) parameters of the disintegrator. The movement of the material in the working chamber of the disintegrator and the change in the concentration of the selected components of the mixture are presented on the basis of the cell mixing model. It allows to determine the concentration of the selected component of the mixture at the outlet of the body of the disintegrator in the tangential discharge pipe. According to expression, the concentration of the selected components of the mixture when passing through the disintegrator body of the presented construction is about half (0.57) of the initial value.