Results are presented for investigation of the movement of free-flowing materials in double-shaft paddle mixers. A method of reducing the mixing times of these free-flowing materials, and the design of the doubleshaft paddle mixer for this reduction, which provides for intensification of mixing due to an additional loop for particle movement are examined. Paddle mixers are widely used in various branches of industry. A number of investigations relative to mixing of freeflowing materials have been conducted in these mixers for the purpose of shortening the time required for preparation of the mixture, and improvement of its quality [1, 2]. Let us isolate two basic types of double-shaft paddle mixers: without intersection of the rotational trajectories of the paddles of the parallel shafts (Fig. 1a); and, with intersecting rotational trajectories of the paddles of the parallel shafts (Fig. 2a). It is proposed to shorten the preparation time of the mixture in the mixers with allowance for charging rules by rapid equalization of the initial components along the tiers of the effective members, intensification of convective and diffusion mixing [3, 4], and organization of large-flow discharge of the mixture without loss of its uniformity due to variation in the rotational direction of the shafts and variation of the position of the paddles on these shafts. Two methods of charging the initial components into the mixer are: uniform charging in order of decreasing sizes (the concentration of initial components in each tier of effective members is essentially the same); and, simultaneous charging via different devices (positioning of the initial components is strictly isolated with respect to the tiers of effective members) [4]. Let us examine a mixer (see Fig. 1a) in the housing of which paddles 2 are located on shafts 1 such that the material is mixed from one terminal section of the mixer in one direction, and to the other terminal section in the other direction, while at the end, one or two pairs of paddles are mounted at the opposite angle for agitation of the mixture in the opposite direction. The rotational trajectory of paddles 2 on shafts 1 do not intersect. The interaxial distance between the shafts a 1 > 2R (R is the radius of the rotational trajectory of the paddles). For the method of simultaneous loading of the initial components, a largeflow counter-movement of particles 3 is formed from one terminal section to the other in the initial stage to equalize their concentration along the shafts in each tier of effective members, and intensify convective mixing (see Fig. 1b). Shafts 1 rotate in opposite directions, displacing the free-flowing material from the center of the mixer toward the lateral walls of the housing. Formation of zones of material slip (A) is possible near the terminal walls of the housing in the mixer, resulting in a nonuniform load over the length of the shaft, and slowing of the process of uniform movement of the material. Movement of material is insignificant between the effective zones of the shafts; this renders equalization of the concentration of initial components difficult within the entire reaction space (see Fig. 1b). Charging requires organization within the central zone along the mixer. The charging consumes from 0.1 to 0.3 of the total time required for mixing. To intensify diffusion mixing, the direction of rotation of the shafts is reversed, mixing the material from the lateral walls of the housing toward the center of the mixer. Active exchange of particles occurs between the opposing flows in the central portion of the mixer (see Fig. 1c).
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