At the present time, continuous-mixing processes, which make it possible to react to deviations from the normal course of an operation, and to regulate these deviations, are used to produce multicomponent powder mixtures. That mixture, when the components for the minimum heterogenous reaction microcell in which they are in the required (assigned) proportion and required (assigned) mutual arrangement dictated by the purpose of the constituent components, can be considered ideal. Nonobservance of these two conditions will result in incomplete utilization of the properties of the components. In chemical sources of electric current of a manganese-zinc system, for example, a total of 60‐70% of the manganese-zinc powder mixture is utilized with respect to computed capacity efficiency, the energy potential of a solid rocket fuel is reduced due to a disturbance in the proportion of the combustible material and oxidizing agent in the minimum reaction cell, and so forth. In ideal heterogeneous cells having the required ratio of concentrations and mutual arrangement of components, it is possible to note a regularity of structure, and, consequently, if the components are delivered in the required proportion as particles (single-layer flow), the requirement is precluded in the mixer for the production of the required cell structure. From this position, the mixer should be treated as a device that compensates for the impossibility of supplying initial particle components at the required output; this reduces the degree of segregation to zero for a single-layer flow. Inconsistencies between the quality of the mixture, the required mixing time, and the output are virtually eliminated, if it is assumed that the overall process of controlled continuous mixture preparation consists of the following stages: continuous metered feed of components with a minimum flow section and required output; continuous restructuring of the flow of components to a single layer flow; and continuous mixing with eventual zero segregation of the mixture [1]. Preparation of the mixture in accordance with the proposed procedure significantly lowers the power consumption of the equipment (kWh/ton of mixture), since the paths of the particles of the components are short for the required quality of the mixture as a result of connection between single-layer flows, whereas in traditional schemes used for mixture preparation, each particle of the components should advance between other particles for an extended time to form a homogeneous mixture; this requires large energy outlays. A process diagram with a thin-wall stacking of flows of powder components will make it possible to diminish the effect of the physical, chemical, and mechanical properties of the material, which frequently impede attainment of the required quality of mixture (when traditional flow diagrams are used). The proposed process flow diagram will make it possible to prepare the powder mixture easily with respect to the differential-variable ratio of proportions between components, and also periodically add a component feed to, or remove it from the preparation process; this may be of special interest to production engineers working in the chemical and foodstuff industries, powder metallurgy, etc. Figure 1 shows a process sequence diagram of the method under consideration for the preparation of multicomponent powder mixtures. All components pass through a preparation process for a metered feed to average-out the