🌪️ Agitator Power & Mixing Time
Compute industrial agitator shaft power draw, specific power (W/m³), liquid pumping rate, and 95% homogenization blending time.
⚡ Fortran 90 Engine
Double Precision (IEEE 754)
✓ ISO / ASME Validated
📊 Solver Telemetry
● ACTIVE
👁️ Consultations
17
⚡ Calculs faits
15
💾 Téléchargements
355
📦 Code Fortran
4.4 KB
📅 Mise en service
Jun 2026
⏱️ Latence
< 1 ms
🌪️ Baffled Mixing Tank Vortex & Turbulent Streamlines
Real-time visual simulation of impeller rotation, liquid pumping flow & tracer dispersion📝 Configuration & Presets
🧪 Rushton Turbine (120 RPM)
🌊 Hydrofoil Flocculator (45 RPM)
🎨 Pitched Blade (850 cP)
🍯 Anchor Impeller (25k cP)
Mixing Formulations:
• Impeller Reynolds: Re = (ρ · N · D²) / μ
• Shaft Power: P = Np · ρ · N³ · D⁵ [Watts]
• Pumping Rate: Qp = Nq · N · D³ [m³/s]
• 95% Mixing Time: θ₉₅ = [ 5.4 / (N · Np⅓) ] · (T/D)²
• Impeller Reynolds: Re = (ρ · N · D²) / μ
• Shaft Power: P = Np · ρ · N³ · D⁵ [Watts]
• Pumping Rate: Qp = Nq · N · D³ [m³/s]
• 95% Mixing Time: θ₉₅ = [ 5.4 / (N · Np⅓) ] · (T/D)²
📊 Agitation & Power Results
Configure inputs and click Compute to view results.
📘 Calculation Methodology & Mixing Theory
Power Draw Scaling Law
Shaft power scales cubically with rotation speed $N^3$ and with the 5th power of diameter $D^5$ in the turbulent regime:
P = Np · ρ · N³ · D⁵
Grenville 95% Mixing Time
The 95% homogenization time $\theta_{95}$ predicts complete batch blending based on turbulent macro-mixing turnover loops.
Key Engineering Assumptions
- Single impeller mounted on central vertical shaft ($C = T/3$ off bottom).
- Standard full liquid volume $H \approx T$.
- Motor safety service factor $SF = 1.25$ applied for viscous startup surges.