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Home / Blog / Absorber Tower: Design Steps, Column Types, Price Factors, Selection and Case Study

Absorber Tower: Design Steps, Column Types, Price Factors, Selection and Case Study

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Author:
Anna Frank, Equipment Selection Expert
Michael-Klepik
To neutralize gases, dust, and aerosols, specialized equipment known as an absorber tower is used. These purification systems are widely applied in the chemical, gas, and metallurgical industries, as well as in paint booths, energy complexes, water treatment facilities, and other sectors.

What Is an Absorber Tower?

The key distinction of the unterschied adsorber absorber tower lies in its operating principle: an adsorber removes impurities by trapping them on the surface of a solid porous material, whereas an absorber column utilizes volumetric absorption by a liquid.

A typical absorber tower schematic consists of a vertical cylindrical vessel made of steel or plastic, a liquid interaction zone, inlet and outlet pipes, a mist eliminator, and a sludge collection sump where the spent liquid accumulates. In operation, the contaminated stream enters the bottom of the column and flows upward, counter-current to the liquid sprayed from above. Upon contact, physical absorption occurs as solid particles are wetted and entrained by the droplets, and soluble gases dissolve in the liquid. If chemical reagents are present, harmful gases undergo a reaction to form neutral or easily removable compounds. The purified stream is then discharged through the top outlet, while the sludge is collected at the bottom for disposal or recirculation.

To ensure stable performance despite fluctuating input conditions, a wet absorber towers control system is employed. This system integrates sensors such as flow meters, pressure gauges, thermocouples, and pH meters, along with actuators like control valves. The controller maintains the optimal gas-to-liquid ratio and precisely doses chemical reagents to guarantee the required purification efficiency.
Venturi-type absorber tower at an industrial site
Venturi-type absorber tower at an industrial site
Exploring the design of a spray absorber tower

Design Steps

Absorber tower design typically involves the following key stages:
  1. Analysis of initial data and definition of requirements, including determining the composition and temperature of the stream, establishing the required purification efficiency, and selecting the appropriate type of irrigation liquid;
  2. Thermodynamic and physicochemical calculations to determine phase equilibrium and absorption kinetics;
  3. Process (hydraulic) calculations to establish the column diameter and height, determine the number and type of nozzles, and select the necessary pumping equipment; to determine the number of plates, an absorber tower diagram (X-Y diagram) is used;
  4. Detailed design calculations, covering the selection of housing material, determination of wall thickness, sizing of supports and flange connections, and design of inlet and outlet components;
  5. Selection of additional auxiliary equipment, such as mist eliminators, reagent dosing systems, liquid recirculation systems, and sludge settling tanks.
Packed Absorber Tower Diagram
Packed Tower Diagram

Selection of Column Type

Gas absorber tower can be categorized into the following types:
  • Packed;
  • Tray (including foam-type trays);
  • Open Spray;
  • Venturi scrubber.
TORNADO FB Venturi Packed Bed Scrubber
Performance:
600 — 30 000 cfm
TORNADO T-RP Dual-Stage
Performance:
100 — 30 000 cfm
TYPHOON Tray Tower Scrubber
Performance:
100 — 175 000 cfm
Wet Venturi Scrubber
Performance:
100 — 175 000 cfm
TORNADO ST Spray Tower Wet Scrubber
Performance:
600 — 30 000 cfm
TORNADO FB Fluidized Packed Bed Scrubber
Performance:
100 — 175 000 cfm
In addition to the basic types, specific designs are also available, such as microoperforierte absorber towers or units equipped with additional features like heating.
Adsorber tower for tank applications at a production site

Price Factors

Several key factors influence the price of absorber tower: the choice of construction material (responsible for up to 60–70% of total cost), the type of column and its internal design (with cost varying by packing or tray configuration), and the physical dimensions. A taller column of the same diameter leads to proportionally higher costs, but a wider diameter drives up the water absorber tower price even more substantially. Additionally, because the design is affected by operating pressure and temperature, extreme conditions—such as pressures exceeding 30 bar or temperatures below -75°C—result in a significant escalation in cost.

Additionally, the overall cost is influenced by the integration of auxiliary equipment. For instance, a refluxed absorber tower requires additional piping for recirculation, a reboiled absorber tower necessitates the integration of heat exchange equipment, and an entrained flow absorber tower demands a highly efficient mist eliminator or entrainment separator. In addition to the primary contact elements (such as plates or nozzles), the overall cost is also influenced by the choice of liquid distributors and mist eliminators.
Tornado FB Tower Overview at a Client Site

Murphree Efficiency

The Murphree efficiency is used to evaluate the performance of a contact device, such as a tray, by measuring how closely the actual change in concentration on a tray approaches the ideal change that would occur if equilibrium were reached—in essence, it represents the tray's efficiency. In practice, a murphree absorber tower efficiency in the range of 60% to 90% or higher is generally regarded as effective. During the design of a column, this metric is employed to determine the required number of trays.
Foam Tower Overview

Absorber Tower Incomplete Mixing

There are situations where some of the gas passes through the column without properly contacting the liquid, leading to a dramatic reduction in purification efficiency. Absorber tower incomplete mixing may result from issues such as liquid failing to uniformly flow through the packing or certain nozzles not producing the intended spray pattern.

This problem can typically be detected by monitoring the outlet stream—for example, if the purified stream contains more impurities than expected or if sudden surges in flow or pressure occur. Resolving the issue requires identifying its underlying cause, which could include clogged nozzles, fouled packing, excessive foaming, or other factors. Corrective action may involve adjusting the operating mode and performing maintenance, such as cleaning contaminated components or replacing faulty parts.
Spray Tower GIF Animation
Spray Tower GIF Animation

FAQ

  • 1. Will standard equipment withstand temperatures ranging from -50°C to +250°C in our process?
    Extremely low temperatures require insulation or the use of antifreeze agents, while extremely high temperatures call for preliminary cooling.
  • 2. What housing material should we choose for aggressive environments?
    Use stainless steel type 12X18H10T; if harsh acids or alkalis are involved, use plastic.
  • 3. Can we install the column outdoors in the northern region?
    Yes, for operation down to -60°C. You will need a housing made of 09G2S steel.
  • 4. Our column performance dropped. Could this be due to incomplete mixing?
    It could be if you notice these symptoms: lower purification efficiency (outlet impurities exceed norms), pressure fluctuations (drop from stream channeling or rise from clogging), or flow surges as automation compensates. During shutdown, inspect for dry spots or clogs.
  • 5. Which type offers the highest cleaning efficiency?
    Venturi scrubbers deliver maximum efficiency when short contact time with the contaminant is sufficient. If a chemical reaction is required, packed columns or foam-type trays are more suitable.
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