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NGL Fractionation Column Sizing

GPSA Β· Plant Processing of Natural Gas Ch. 9 Β· Distillation Design

NGL Fractionation Column Sizer
Size deethanizer, depropanizer, debutanizer, and butane splitter columns using Fenske-Underwood-Gilliland (FUG) shortcut method per GPSA. Calculates theoretical stages, minimum/operating reflux ratio, column diameter (Fair correlation), feed tray location (Kirkbride), and heat duties.

Column Type & Operating Conditions

BPD
psia
GPSA typical: 180-300 psia for depropanizer

Product Specifications

mol%
mol%
HD-5 propane: β‰₯95% C₃, ≀2.5% Cβ‚„+

Feed Composition (Binary/Pseudo-binary)

mol%
mol%
FUG method assumes binary/pseudo-binary separation. For multicomponent feeds, use rigorous simulation.

FUG Shortcut Method

This calculator uses the Fenske-Underwood-Gilliland (FUG) shortcut method per GPSA Section 19:

  • Fenske: Minimum stages at total reflux (Nmin)
  • Underwood: Minimum reflux ratio (Rmin)
  • Gilliland: Actual stages at operating reflux
  • Fair: Column diameter from vapor loading
  • Kirkbride: Optimal feed tray location

GPSA Typical Operating Ranges

  • Deethanizer: 250-450 psia, 30-50 trays, Ξ± β‰ˆ 2.5-3.0
  • Depropanizer: 180-300 psia, 25-40 trays, Ξ± β‰ˆ 2.2-2.6
  • Debutanizer: 60-150 psia, 20-35 trays, Ξ± β‰ˆ 2.0-2.4
  • Butane Splitter: 100-200 psia, 80-120 trays, Ξ± β‰ˆ 1.1

Design Notes

  • Reflux ratio: R = 1.1-1.3 Γ— Rmin is economic optimum
  • Tray efficiency: O'Connell correlation gives Ξ· = 0.70-0.85
  • Diameter sizing: Design at 75-85% of flooding velocity
  • Tray spacing: 24" standard for NGL; 18" for small columns
  • Pressure drop: ~0.1-0.2 psi per tray typical

Limitations

  • FUG assumes constant relative volatility (Ξ± Β± 20%)
  • Results are Β±10-20% for preliminary design
  • Multicomponent feeds require rigorous simulation
  • Verify with HYSYS/Aspen before final design