Emulsifying Tank Droplet Breakup: Rotor-stator Shear, Turbulence And Micro Droplet Formation

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Droplet size decides whether an emulsion stays smooth or separates within days. In an emulsification tank, that size is set inside a narrow zone around the rotor, where each droplet meets forces strong enough to tear it apart.

Definition: Droplet Breakup in a Rotor-Stator Tank

An emulsifying tank reduces droplet size through a high-speed rotor-stator assembly. The spinning rotor generates intense shear, centrifugal force and hydraulic impact, which tear large droplets into micro droplets and spread them evenly through the continuous phase.

Four Stages From Large Droplet to Micro Droplet

  1. Rotor acceleration: The rotor spins at tip speeds of roughly 15–40 m/s, drawing liquid axially into the head and accelerating it outward toward the stator.

  2. Gap shear: Fluid enters the narrow shear gap, where steep velocity gradients stretch each large droplet into an elongated thread that becomes unstable and pinches into fragments.

  3. Slot discharge: Centrifugal force pushes the stretched fluid through stator slots as high-velocity jets, which collide with slower bulk liquid and add a further round of hydraulic impact.

  4. Recirculation: Discharged liquid returns to the inlet, so every droplet passes through the head many times until the size distribution narrows to the target range.

Physics of Droplet Rupture

Weber Number and Interfacial Tension

Interfacial tension holds a droplet together, while turbulent stress tries to deform it. The ratio of these forces is the Weber number, and a droplet splits once that ratio exceeds a threshold.

Hinze's turbulence model ties maximum stable droplet size to energy dissipation rate ε, following d_max ∝ ε^−0.4. Doubling local dissipation cuts the largest droplet diameter roughly 24 percent, provided droplets stay above the Kolmogorov scale.

Shear Force in the Gap

Inside an emulsifying tank, velocity differences across a 0.2–1 mm gap produce shear rates above 20,000 s⁻¹. Droplets elongate, thin into filaments, and rupture once viscous stress overcomes interfacial tension.

Centrifugal Force Through the Stator

Rotation throws liquid radially outward through the stator slots at high velocity. This pumping action also draws fresh material into the head, keeping the dispersed phase circulating instead of settling.

Hydraulic Impact and Turbulent Eddies

Jets leaving the slots strike slower bulk liquid and the vessel wall, creating turbulent eddies and pressure fluctuations. Eddies near the droplet scale apply uneven stress and split it further.

Operating Variables That Set Final Droplet Size

The table lists typical starting ranges for rotor-stator systems. Actual values shift with formulation, viscosity and batch volume, so trial runs remain necessary before scale-up.

Variable Typical Range Effect on Droplet Size
Rotor tip speed 15–40 m/s Higher speed reduces droplet size
Shear gap width 0.2–1.0 mm Narrower gap raises shear rate
Batch turnovers 3–10 More passes narrow the distribution
Emulsifier level 0.5–5 % Faster interface coverage limits merging

One rotor-stator stage typically yields a Sauter mean diameter of 1–10 µm. Sub-micron targets usually require a second stage, such as a high-pressure homogenizer, after pre-emulsification in the emulsifying tank.

Design Features That Influence Dispersion

Stator geometry in an emulsification tank matters as much as speed. Fine slots narrow the size distribution, coarse teeth handle viscous pastes, and vacuum operation limits air entrainment that would otherwise absorb energy.

Troubleshooting Oversized Droplets

Oversized droplets in an emulsification tank usually trace back to four causes, and each has a direct adjustment that can be tested during a trial batch.

  1. Coarse droplets: Raising rotor speed in 10 percent steps, while staying within the rated tip speed, increases energy dissipation and directly lowers the maximum stable droplet size.

  2. Wide size distribution: More batch turnovers or a tighter gap narrows the spread, and an anchor agitator improves bulk circulation, so no region of the batch skips the shear head.

  3. Coalescence after mixing: A higher emulsifier level or a surfactant with a suitable HLB value stabilizes the interface, since droplets with incomplete coverage merge soon after leaving the shear zone.

  4. Temperature drift: Steady jacket temperature control matters because viscous dissipation raises batch temperature noticeably, which alters viscosity, interfacial tension and breakup behavior during extended runs.

Practical Takeaways for Droplet Control

Rotor speed sets energy input, shear and impact break droplets down, and emulsifier coverage keeps them separate. A well-specified emulsifying tank adds controlled recirculation and stable temperature.

Emulsifying Tank Droplet Breakup: Rotor-stator Shear, Turbulence And Micro Droplet Formation

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