Lapple cyclone

Select calculation method

Input data

Bulk Flow

Total flowAUTO

Granulometry

Size class
Units
Retained
+100Oversize
kg/h
-100 +508.0%
kg/h
-50 +2024.0%
kg/h
-20 +1026.0%
kg/h
-10 +522.0%
kg/h
-5 +212.0%
kg/h
-2 +14.0%
kg/h
-1Pan
kg/h

Cut diameter (d50)

Output data

Bulk Flow

Total flowAUTO

Granulometry

Size class
Units
Retained
+100Oversize
kg/h
-100 +500.0%
kg/h
-50 +200.0%
kg/h
-20 +100.0%
kg/h
-10 +50.0%
kg/h
-5 +20.0%
kg/h
-2 +10.0%
kg/h
-1Pan
kg/h

Bulk Flow

Total flowAUTO

Granulometry

Size class
Units
Retained
+100Oversize
kg/h
-100 +500.0%
kg/h
-50 +200.0%
kg/h
-20 +100.0%
kg/h
-10 +50.0%
kg/h
-5 +20.0%
kg/h
-2 +10.0%
kg/h
-1Pan
kg/h

Overall collection efficiency

Collected dust

Dust escaping with the gas

Description

Reverse-flow cyclone of standard Lapple proportions, for gas–solid separation. Every dimension is a fixed multiple of the body diameter DcD_c, which makes the Lapple model the classical basis for the preliminary design of dust cyclones.

Lapple cycloneLapple cyclone

Calculation methods

  • Sizing for a target cut size: body diameter and number of cyclones in parallel required to reach a given cut size within the maximum inlet velocity and pressure drop; also the pressure drop, blower power and principal dimensions.
  • Dimensions: cut size, inlet velocity, pressure drop, blower power and principal dimensions of a cyclone of known diameter.
  • Grade efficiency curve: collection efficiency as a function of particle size.
  • Dust split from the cyclone diameter and from the cut diameter: division of a particle size distribution into the collected (underflow) and escaping (overflow) streams, with the overall collection efficiency.

Model

For NN identical cyclones in parallel, each receiving q=Q/Nq = Q/N:

Vi=qHW=8qDc2d50=9μW2πNeVi(ρp−ρ)=3μDc3128πq(ρp−ρ)V_i = \frac{q}{H W} = \frac{8 q}{D_c^2} \qquad d_{50} = \sqrt{\frac{9 \mu W}{2 \pi N_e V_i (\rho_p - \rho)}} = \sqrt{\frac{3 \mu D_c^3}{128 \pi q (\rho_p - \rho)}}

ΔP=NHρVi22, NH=8η(d)=11+(d50/d)2\Delta P = N_H \frac{\rho V_i^2}{2},\ N_H = 8 \qquad \eta(d) = \frac{1}{1 + (d_{50}/d)^2}

where ViV_i is the inlet velocity, Ne=6N_e = 6 the number of effective turns, NH=KHW/De2N_H = K H W / D_e^2 the number of inlet velocity heads (K=16K = 16), ρp\rho_p and ρ\rho the particle and gas densities and μ\mu the gas viscosity. Standard proportions: L1=L2=2DcL_1 = L_2 = 2D_c, H=De=Dc/2H = D_e = D_c/2, W=Dd=Dc/4W = D_d = D_c/4, L3=5Dc/8L_3 = 5D_c/8.

Design criteria

  • Inlet velocity between 15 and 25 m/s and pressure drop up to 2.5 kPa; both limits may be changed under Design coefficients. With NH=8N_H = 8, a pressure drop of 2.5 kPa in air corresponds to an inlet velocity of about 23 m/s, so the pressure limit generally governs the sizing.
  • Default properties: air at 20 °C and 1 atm, quartz particles (2650 kg/m³).
  • The model neglects mass loading and bypass and tends to overestimate the collection of the finest particles; it is intended for preliminary design.

References

  • LAPPLE, C. E. Processes use many collector types. Chemical Engineering, v. 58, n. 5, p. 144-151, 1951.
  • SHEPHERD, C. B.; LAPPLE, C. E. Flow pattern and pressure drop in cyclone dust collectors. Industrial & Engineering Chemistry, v. 31, n. 8, p. 972-984, 1939.
  • COOPER, C. D.; ALLEY, F. C. Air Pollution Control: A Design Approach. 4. ed. Long Grove: Waveland Press, 2011.
  • CIMBALA, J. M. Lesson 12B: Lapple Cyclone. A Practical Application of Inertial Separation.