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Packed Column Design Calculator

GPSA · Plant Processing of Natural Gas Ch. 9 · Packed Towers

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Packed Tower Design Calculator
Designs packed absorption and distillation columns using random or structured packing. Calculates column diameter, packing height, pressure drop, and loading limits per manufacturer correlations.

Process Conditions

MMSCFD
gpm
psia
°F

Fluid Properties

lb/ft³
lb/ft³
cP

Packing Selection

Random Pall Rings: Good capacity, moderate cost, wide application

About Packed Columns

Packed columns use structured or random packing instead of trays for vapor-liquid contact. They offer advantages in pressure drop, liquid holdup, and turndown capability compared to tray columns.

Packing Types

  • Random Packing: Dumped in bulk, lower cost, easier installation
  • Structured Packing: Engineered geometry, higher efficiency, lower ΔP
  • Metal: Higher capacity, better for high pressure
  • Ceramic/Plastic: Corrosion resistant, lower cost

Design Guidelines

  • Flooding: Design for 70-80% of flood velocity
  • Turndown: 3:1 to 5:1 typical
  • Minimum Wetting: 3-5 gpm/ft² for random packing
  • ΔP: 0.2-0.5 in H₂O/ft typical

Advantages vs. Trays

  • Lower pressure drop (important for vacuum service)
  • Better turndown capability
  • Lower liquid holdup (important for corrosive/reactive systems)
  • Can handle solids better (structured packing)

Disadvantages vs. Trays

  • More difficult to predict performance
  • Liquid distribution critical
  • Inspection and maintenance more difficult
  • Can be more expensive (structured packing)
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