Lapple cyclone

Select calculation method

Input data

Gas flow (total)

Target cut diameter (d50)

Particle density

Gas density

Gas viscosity

Blower efficiency

Minimum inlet velocity

Maximum inlet velocity

Maximum pressure drop

Output data

Cyclones in parallel

Cyclone diameter (Dc)

Inlet velocity

Pressure drop

Blower power

Body height (L1 = 2Dc)

Cone height (L2 = 2Dc)

Inlet height (H = Dc/2)

Inlet width (W = Dc/4)

Gas outlet diameter (De = Dc/2)

Vortex finder length (L3 = 5Dc/8)

Dust outlet diameter (Dd = Dc/4)

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.