Introduction & Context

The Reynolds number for mixing systems is a dimensionless group that quantifies the ratio of inertial to viscous forces within an agitated vessel, serving as the primary correlating parameter for Reynolds number matching, scaling operations, predicting power draw, and selecting impeller geometry. When evaluating overall equipment performance, the surface finish of mixing equipment plays a crucial role in minimizing frictional losses and ensuring consistent flow regimes, especially in high‑viscosity polymers, fermentation broths, slurries, and non‑Newtonian fluids where flow behavior directly impacts heat and mass transfer rates and mixing times.

Methodology & Formulas

  1. Convert rotational speed
    Impeller speed is usually supplied in revolutions per minute (RPM). Convert to radians per second (s-1) via: \[ N = \frac{N_{\text{RPM}}}{60} \]
  2. Convert dynamic viscosity
    Viscosity is frequently reported in centipoise (cP). Convert to pascal-seconds (Pa·s) while preventing non-physical zero values: \[ \mu = \max\left( \mu_{\text{cP}} \times 0.001,\; 1\times10^{-9} \right) \]
  3. Compute the Reynolds number
    The general definition for pipe flow is adapted to agitated systems by replacing the characteristic length with the impeller diameter: \[ Re = \frac{\rho\,N\,D^{2}}{\mu} \] where:
    • \( \rho \) = fluid density (kg·m-3)
    • \( N \) = impeller rotational speed (s-1)
    • \( D \) = impeller diameter (m)
    • \( \mu \) = dynamic viscosity (Pa·s)
  4. Determine flow regime
    The calculated Reynolds number is compared against standard thresholds for mechanically agitated systems:
    Reynolds Number Range Flow Regime
    \( Re < 10 \) Laminar
    \( 10 \le Re < 10\,000 \) Transitional
    \( Re \ge 10\,000 \) Turbulent