is forced both under the input pressure and centrifugal force outwardly through the radial apertures 76 of the skirt 77 into the three pressure zones 64 formed between the kinetic baffles 58 the turbine blade 66 causes the material to rotate and to move outwardly in each of the three pressure zones 64 the second material is introduced through the secondary inlet 54 in one pressure zone between the baffles the baffles 58 prevent the two materials from merely being moved as a swirling mass and around the turbine blade 66 a small amount of material is permitted to rotate from pressure zone to pressure zone 64 of the lower chamber by way of the apertures 62 in the baffles once directed outwardly by the turbine blade 66 the input pressure of the materials is such that it moves the combined materials upwardly through the aperture 44 in the baffle plate 40 and alongside of the shaft 46 clearance between the shaft 46 and baffle plate 40 is such that the material is sheared as in the static mixing the combined phase materials are then moved into the upper chamber 42 where the second blade 80 forces the material outwardly and through the fine porous screen 84 the rotation causes dynamic mixing and the screen 84 imparts energy by way of shear as the materials move through the screen 84 the porosity of the screen 84 may be controlled and coordinated with the nature of the materials being dispersed in regard to the embodiment shown is fig5 the baffles 158 are disposed to induce a counterrotation of the fluids being mixed the baffles 159 on the chamber separator induce rotation to the liquid before it passes through the.