⬇️ Sedimentation & Terminal Velocity Calculator

Compute terminal settling velocity for particles through Stokes, intermediate (Schiller-Naumann), and Newton drag regimes. Includes shape correction, Archimedes number, hindered settling, and CD vs Re diagram.

🔬 Particle Settling Schematic

📝 Configuration

⚫ Particle Properties
ϕ < 1 increases drag for non-spherical particles.
💧 Fluid Properties
📊 Concentration (hindered settling)
0 for single-particle settling.
Key Equations:

Stokes: Vt = (ρp−ρf)gd²/(18μ)
Schiller-Naumann: CD = 24/Re(1+0.15Re0.687)
Newton: CD = 0.44
Richardson-Zaki: Vh = Vt(1−c)n
Ar = ρfp−ρf)gd³/μ²

📊 Results

Configure inputs and click Compute to view results.

📘 Methodology

Drag Regimes

Three classical regimes: Stokes (Re < 0.1) with CD = 24/Re, intermediate (0.1 < Re < 1000) using Schiller-Naumann correlation, and Newton (Re > 1000) with CD ≈ 0.44. The engine iterates to convergence.

Hindered Settling

Richardson-Zaki correlation accounts for particle-particle interactions in concentrated suspensions: Vh = Vt(1−c)n, where n depends on Rep.

Assumptions

  • Spherical particle (shape factor adjusts drag).
  • Steady terminal velocity (no acceleration phase).
  • Infinite fluid domain (no wall effects).
  • Newtonian fluid.
  • No particle rotation or lift.
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