Skip to main content

Packed Bed Absorption Column HTU-NTU Height Calculator

Packed absorption columns remove dilute pollutants or recover volatile gases by continuous counter-current contact with liquid absorbents.

Superficial gas mass flow flux.

Superficial solvent liquid mass flow flux.

Entering gas-phase solute concentration.

Cleaned gas exit solute concentration.

Henry law equilibrium solubility line slope.

Overall gas-side mass transfer coefficient times packing area.

Calculated Result
3.71 m

Required Packing Bed Height

Transfer Units (N_OG)

3.24

HTU (H_OG)

1.14 m

Absorption Factor (A)

2.57

Calculation Breakdown

  1. Absorption Factor (A = L / mG)3.5 / (0.85 · 1.6) = 2.574
  2. Number of Transfer Units (N_OG)Colburn equation = 3.24 stages
  3. Height of a Transfer Unit (H_OG)G / (K_OG·a) = 1.143 m
  4. Total Required Packing Height (Z)Z = N_OG · H_OG = 3.24 · 1.143 = 3.71 m

What Is the Packed Bed Absorption Column HTU-NTU Height Calculator?

The HTU-NTU method models continuous differential mass transfer columns where gas and liquid streams remain in uninterrupted contact along packing surfaces.

How Does the Packed Bed Absorption Column HTU-NTU Height Calculator Work?

NTU measures the degree of separation difficulty; HTU represents the physical packing efficiency; their product gives total required packing height.

Packed Bed Absorption Column HTU-NTU Height Calculator Formula & Variables

The core mathematical equation utilized by this calculator is expressed as:

Z = N_{OG} imes H_{OG}, quad N_{OG} = rac{lnleft[ rac{y_1}{y_2}left(1 - rac{1}{A} ight) + rac{1}{A} ight]}{1 - rac{1}{A}}, quad A = rac{L}{m G}

Colburn dilute absorption equation for Number of Transfer Units and total packed bed height.

How to Use the Packed Bed Absorption Column HTU-NTU Height Calculator

  1. Input gas and liquid velocities, inlet/outlet solute mole fractions, equilibrium line slope m, and volumetric mass transfer coefficient.

Step-by-Step Example Calculation

Scrubbing VOC from Industrial Exhaust Stream

Input Values:

gasMassFluxKgM2S:1.6
liquidMassFluxKgM2S:3.5
inletGasMoleFractionY1:0.045
outletGasMoleFractionY2:0.004
equilibriumSlopeM:0.85
overallKogMolM3S:1.4
Worked Steps: Absorption factor A = 2.57, Transfer units N_OG = 2.92, HTU H_OG = 1.14 m, Packed height Z = 3.34 m.

Understanding Your Result

Displays required packing height Z in meters, number of transfer units N_OG, HTU in meters, and absorption factor A.

Factors That Affect the Result

  • Operating with absorption factor A = L/(m*G) between 1.4 and 2.0 optimizes column height against solvent recirculation costs.

When Should You Use This Calculator?

  • Air pollution wet scrubbers, amine acid gas sweetening, ammonia stripping, and bioprocess off-gas treatment.

Assumptions & Limitations

  • Applies to dilute isothermal gas streams with linear Henry equilibrium solubility lines.

Frequently Asked Questions

Calculation Accuracy & Reference Note

Standard chemical engineering mass transfer formulation.

Explore more tools and calculators in Chemistry Calculators