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Performance considerations in stator selection for high shear rotor-stator mixers
okozyuk.com
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5. Selection by emulsification duty
5.1 Pre-emulsion formation
For pre-emulsion duty, where the goal is to disperse one liquid phase into another before final droplet size reduction, a square hole or slotted stator is often the preferred first stage geometry. These heads generate enough shear to achieve initial dispersion while maintaining strong macrocirculation through the vessel. That balance becomes important when the oil phase is introduced rapidly or when system viscosity increases during inversion, since excessive restriction can reduce turnover and destabilize the process.
5.2 Final droplet refinement
For final droplet size reduction, the stator selection should move toward finer perforation patterns or multistage shear geometries. These configurations raise local shear rates, increase the frequency of droplet disruption events, and improve exposure to repeated shear, which supports smaller mean droplet size and a narrower particle size distribution.
5.3 Shear sensitive emulsions
Not all emulsions respond favorably to maximum shear intensity. In shear sensitive systems, excessive local energy dissipation can cause thermal rise, structural breakdown, or destabilization of the dispersed phase. In these cases, a slotted or square hole stator that provides moderate but sustained shear can outperform a fine emulsor geometry by preserving product structure while still delivering adequate dispersion and stability.
5.4 High internal phase or viscosity rising emulsions
For emulsions with a high internal phase ratio, or for systems in which viscosity rises rapidly during processing, stator selection must preserve macrocirculation throughout the vessel rather than maximize local shear alone. A common failure mode is selecting a fine stator too early, producing excellent shear intensity in the immediate rotor-stator zone but insufficient bulk turnover, which limits phase distribution and can stall the process. A more robust approach is to start with coarser stator geometry to establish uniform dispersion and circulation, then transition to a finer head only after the phases are well distributed. This is a practical process inference consistent with vendor guidance that emphasizes the need to balance shear generation with vessel scale circulation, particularly in high viscosity systems where sweep agitation may also be required.