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Caustic Scrubber for H2S Removal
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Caustic Scrubber for H2S Removal

Caustic Scrubber for H2S Removal

Item: Caustic Scrubber for H₂S Removal
Capacity: 100 ~ 50,000 Nm³/h
Operating Pressure: 0.1 ~ 6.0 MPaG
H₂S Removal Efficiency: ≥99%

product Introduction

 

The Caustic Scrubber for H₂S Removal is an industrial gas treatment system, widely used in natural gas processing, refinery off-gas treatment, biogas upgrading, and industrial acid gas purification.

China Caustic Scrubber For H2s Removal

 

Key Features

 

  1. Packed or tray tower with countercurrent gas-liquid contact.
  2. Knockout drum upstream for bulk liquid and particle separation ≥ 5 μm.
  3. Mist eliminator at gas outlet for droplet removal.
  4. Closed-loop circulation system with pump-driven spray distribution.
  5. NaOH concentration control range 2–10% in circulation loop.
  6. Tower material: FRP or 316L stainless steel for alkaline service.
  7. PLC-based system for flow, pH, and circulation parameter control.

 

Working Principle

 

Step 1: Gas Pre-Treatment
A knockout drum removes liquid droplets and solid particles.
Inlet gas conditioning before absorption section.

Step 2: Counter-Current Absorption
Gas flows upward through a packed or tray tower.
An NaOH solution flows downward via a spray system.
Gas–liquid mass transfer in packed zone.

Step 3: Chemical Reaction
H₂S reacts with NaOH, forming Na₂S / NaHS.
Irreversible absorption in liquid phase.

Step 4: Liquid Circulation
Absorbent recirculated by circulation pump system.
Continuous purge maintains NaOH concentration ≥2%.

Step 5: Clean Gas Outlet
Mist eliminator removes entrained liquid droplets.
Treated gas is discharged to the downstream system.

 

Industrial Application Scenarios

 

  • Natural gas sweetening plants
  • Refinery off-gas treatment systems
  • Biogas upgrading and purification
  • Petrochemical gas treatment units
  • Landfill gas desulfurization
  • Industrial acid gas emission control

 

Engineering Design & Customization Capability

 

Design Inputs:

  • H₂S concentration and variability
  • Gas flow rate (Nm³/h)
  • CO₂ content
  • Operating pressure and temperature
  • Required outlet emission limit

Engineering Methods:

  • Process simulation (Aspen Plus / HYSYS)
  • Mass transfer efficiency calculation
  • Hydraulic design (flooding / pressure drop control)
  • Packing selection optimization

 

Comparison with Other H₂S Removal Technologies

 

Technology

Principle

Strength

Limitation

Caustic Scrubber

Chemical absorption (NaOH/KOH)

Fast response, high efficiency

Chemical consumption

Amine System

Regenerative absorption

CO₂ + H₂S removal

Complex regeneration system

Activated Carbon

Physical adsorption

Simple operation

Low capacity

Claus Process

Sulfur recovery

Sulfur recovery

High CAPEX, large-scale only

 

Manufacturing, Testing & Delivery

 

  • Process and mechanical design
  • Fabrication (ASME / GB150 compliance)
  • Factory Acceptance Test (FAT)
  • 72-hour continuous performance testing
  • Site installation guidance
  • Commissioning support

 

FAQ

 

Q: What type of gas streams is a Caustic Scrubber not suitable for?
A: Gas streams requiring sulfur recovery or ultra-low H₂S removal below adsorption-based treatment range.

Q: How is spent caustic solution handled in the system?
A: Spent solution containing Na₂S/NaHS is discharged via controlled purge and treated by oxidation or external neutralization depending on the site wastewater system.

Q: Can the system operate under fluctuating H₂S inlet concentrations?
A: Yes. The system operates under variable load conditions with circulation and dosing control to maintain stable performance.

Q: What factors influence NaOH consumption in operation?
A: NaOH consumption is determined by inlet H₂S load, gas flow rate, and liquid–gas contact conditions.

Q: What upstream gas quality conditions are required for stable operation?
A: Gas must be pre-treated to remove bulk liquids and solids using a knockout drum or equivalent separation unit.

 

 

 

 

 
 

 

 

 

 

 
 

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