Gas-Liquid Scrubber Cyclone | Souders-Brown Sizing | Cyclogen5D

1. Geometry Parameters

Body Diameter (Dc)

mm

De / Dc (vortex finder)St 0.50

a / Dc (inlet height)St 0.50

b / Dc (inlet width)St 0.20

S / Dc (VF depth)St 0.50

h / Dc (cylinder height)St 1.50

H / Dc (total height)St 4.00

B / Dc (cone tip)St 0.375

2. Operating Conditions

Inlet Velocity (Vi)

m/s

Gas Pressure

bar

Temperature

°C

3. Fluid Pair

—

ρ_gkg/m³

P_refbar

ρ_lkg/m³

μ_gPa·s

σN/m

4. Computed Dimensions

De—

a (inlet H)—

b (inlet W)—

S (VF depth)—

h (cyl height)—

H (total)—

H_cone—

B (tip dia)—

L/D ratio—

Inlet area—

Re (inlet)—

5. Flow Estimates

Q (m³/s)—

Q (Am³/h)—

Mass flow—

Mach number—

6. Separation Performance

d50 Lapple—

d50 Leith-Licht—

d50 Barth—

d50 Average—

Vortex exponent n—

Override n

Lapple m=2.0 · Barth m=3.5

7. Pressure Drop & Energy

ΔP Shepherd-Lapple—

ΔP Casal-Martinez—

Eu (S-L) = K_SL—

Eu (C-M) = K_CMB—

Shaft power—

Specific energy—

8. Liquid Loading

Inlet liquid vol. fraction

%

Liquid mass flow—

V_wall (tangential)—

V_max (Souders-Brown)—

Vi / V_max—

9. Multi-Stage Cascade

Number of stages

Cascade d50—

Total ΔP—

Overall removal—

10. Feed Droplet Size Distribution

DSD median

µm

Geometric std dev (σg)

Bulk removal efficiency—

11. Sizing From Spec

Target d50

µm

Target Q

m³/s

12. Multicyclone Arrangement

Number of cyclones (N)

Per-unit Dc—

Per-unit d50—

Bundle ΔP—

13. Turndown Check

Flow fraction

Turndown Vi—

Turndown d50—

Turndown V_wall—

14. Multi-Objective Optimization

15. Export

16. Process Flow Schematic

Turndown: d50 & V_wall vs Flow

Scale-Up: d50 vs Dc (fixed ratios)

Pareto Front: d50 vs ΔP

Grade Efficiency Curve