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Cyclone Separator Calculator

Design gas-solid cyclone separators with cut diameter and efficiency calculations

Cyclone Geometry

Standard efficiency — good balance of collection & ΔP

Operating Conditions

Typical: 15–20 m/s

Suggested for flow: 0.43 m

Fluid & Particle Properties

Dust: 2500, Coal: 1300, Cement: 3000

Air at 20°C: ρ=1.2 kg/m³, μ=1.8×10⁻⁵ Pa·s

Lapple (Standard Efficiency)

Inlet a×b: 215×108 mm
Exit Ø: 215 mm
Cylinder h: 860 mm
Total H: 1720 mm
Area Ai: 23112 mm²

Cut Diameter d₅₀

0.00μm

Pressure Drop

489.5573Pa

ΔP

1.97inH₂O

Actual Inlet Vi

12.0m/s

Performance Metrics

Separation Factor

34.3G

Number of Turns

8.0

Reynolds Number

344531

Inlet Area

23112mm²

Collection Efficiency vs Particle Size

1 μm

100.0%

2 μm

100.0%

5 μm

100.0%

10 μm

100.0%

20 μm

100.0%

50 μm

100.0%

100 μm

100.0%

200 μm

100.0%

Grade Efficiency Curve

d₅₀=0.0μm1251020501002000255075100Particle Size (μm)Efficiency (%)

Design Recommendations

Excellent for fine particles (d₅₀ = 0.0 μm)
ΔP = 490 Pa — low pressure drop
Inlet Vi = 12.0 m/s — good range (10–25 m/s)

About Cyclone Separators

Cyclone separators use centrifugal force to separate particles from gas streams. The cut diameter (d₅₀) represents the particle size collected at 50% efficiency, calculated using Lapple's formula. Collection efficiency follows the Lapple efficiency curve: η = 1 / (1 + (d₅₀/dp)²). Higher inlet velocity and smaller diameter improve separation but increase pressure drop.