🏗️

Distillation Tray Hydraulics Calculator

Fair's Correlation · GPSA Section 19 · FRI Guidelines

Distillation Tray Hydraulics Calculator
Comprehensive tray analysis including flooding (Fair's correlation), pressure drop, downcomer backup, weeping, and entrainment. Uses industry-standard methods from GPSA Section 19, Kister's Distillation Design, and FRI correlations.

Tower Geometry

ft
in
%
%
Typical Values:
Active area: 70-85% · Hole area: 8-14%
Tray spacing: 18-24" (standard)

Operating Conditions

lb/hr
lb/hr
psia
°F
Note: L/V ratio affects flooding correlation. Higher L/V requires lower vapor velocity.

Physical Properties

lb/ft³
lb/ft³
dyne/cm
in
Fair's CSB Equation:
CSB = K₁ × (σ/20)^0.2
σ baseline = 20 dyne/cm (hydrocarbon)

About This Calculator

Analyzes sieve tray hydraulic performance for distillation, absorption, and stripping towers using industry-standard correlations.

Key Methods:

  • Flooding: Fair's CSB correlation with K₁ factor from GPSA Fig. 19-14
  • Pressure Drop: Dry tray + liquid head + residual (Kister method)
  • Aeration: Bennett correlation for froth density
  • Weeping: Lockett-Banik minimum velocity
  • Entrainment: Hunt correlation (modified)

Design Targets:

  • Operate at 70-85% of flood
  • Downcomer backup <50% of spacing
  • Entrainment <10%
  • Weeping margin >20%

Quick Reference

Sieve tray ΔP 2-4 in H₂O
Valve tray ΔP 2-5 in H₂O
Weir height 2-3 in typical
Turndown (sieve) 2-3:1
Turndown (valve) 5-8:1

Frequently Asked Questions

What does the tray hydraulics calculator analyze?

It calculates distillation tray hydraulics including weir loading, downcomer flooding, pressure drop, weeping, and entrainment using Fair's flooding correlation and GPSA methods.

What standards and methods are used for tray hydraulic calculations?

The calculator uses Fair's flooding correlation, GPSA methods, and FRI (Fractionation Research Inc.) guidelines for distillation column tray design.

What tray performance issues can this calculator identify?

It identifies flooding, weeping, excessive entrainment, and downcomer backup issues that affect distillation column performance.