Sulphur Tail Gas Thermal Oxidizer

Sulphur Control Without Compromise

Contact Us
Thermal oxidizer system for treatment of sulphur tail gas and destruction of residual sulphur compounds.

Overview

CRA’s Sulphur Tail Gas Thermal Oxidizers are engineered to provide reliable, high-efficiency destruction of reduced Sulphur compounds, such as H₂S, COS, and CS₂, commonly found in Claus unit tail gas and Sulphur recovery processes. Operating at high temperatures with optimized residence times, our systems ensure complete oxidation and stable performance under variable process loads. Built with corrosion-resistant materials, high-integrity refractory linings, and optional heat recovery or pre and post scrubber integration, these oxidizers meet strict environmental standards for SO₂, NOₓ, CO, and unburnt hydrocarbons.

Sub Categories
No items found.

Key Benefits

Here’s how they keep your operations safe, efficient, and

1
>99.9% Destruction Efficiency

Total oxidation of sulphur-bearing compounds, including H₂S, COS, and mercaptans

2
Designed for High Temperature

Operates at 1200–2700 °F (650–1480 °C) depending on sulphur load and process design

3
Engineered with Precision

Detailed CFD, process simulations, and strict QC guarantee adequate residence times and high DRE

4
Handles Variable Load Conditions

Engineered to absorb load swings from SRU upsets, start-ups, or shutdowns with stable combustion

5
Pre and Post Combustion Scrubbing

Advanced pre- and post-combustion scrubbing technologies engineered to meet the specific needs of each application

The CRA Edge

With decades of flare system expertise, CRA goes beyond equipment — we deliver full solutions.

Proven Expertise

With 30+ years of combustion design experience, CRA delivers oxidizers built for extreme sulfur service

In-House Capability

Thermal modelling, materials R&D, and fabrication all under one roof ensure speed and precision

Global Compliance

ISO 9001, ASME Standards, API, and CE

Reliable Performance

Engineered for uptime, safety, and long service life in the harshest industrial environments

Applications

See how we turn hard problems into high-performance infrastructure.

SRU Tail Gas
Claus Plant Off-Gas
Thermal Reactors (Reaction Furnace Exhaust)
Amine Unit Off-Gas
Sulphur-Rich Off-Gas from Petrochemical Units
Acid Gas from Gas Treating

Our Clients

Our Resources

Get all the technical details and resources you need in one place.

Tecnical Datasheet
Download
Tecnical Datasheet
Download
Tecnical Datasheet
Download
Tecnical Datasheet
Download

Frequently Asked Questions

Get all the technical details and resources you need in one place.

When is a Sulphur Tail Gas Thermal Oxidizer the best choice?

This system is best suited for Claus unit tail gas and sulphur recovery operations handling H₂S, COS, CS₂, and mercaptans. It is widely used in:

 

Key Applications:

 

  • Refineries - Claus sulphur recovery unit tail gas treatment
  • Gas processing plants - Sour gas sweetening operations
  • Petrochemical facilities - Sulphur-bearing process vents
  • Hydrogen plants - PSA off-gas with sulphur species
  • Chemical manufacturing - Processes using or producing sulphur compounds

 

System Purpose:

 

  • Final destruction of reduced sulphur compounds to meet environmental limits
  • Convert H₂S, COS, CS₂ to SO₂ (which can be scrubbed or meets direct emission limits)
  • Handle variable SRU loads during start-ups, shutdowns, and upset conditions
  • Reliable backup to sulphur recovery processes

 

Why Specialized Equipment Is Required:

 

  • Corrosive environment - H₂S and SO₂ attack standard materials
  • Variable sulphur loading - Wide range from normal to upset conditions
  • High operating temperatures - Ensure complete sulphur compound oxidation
  • Regulatory stringency - Very low SO₂, NOx, and unburnt hydrocarbon limits

How do sulphur tail gas thermal oxidizers handle variable SRU loads?

They are designed to absorb load fluctuations during start-ups, shutdowns, and upset conditions using stable combustion design, high-integrity refractory systems, and advanced control strategies tailored for sulphur service.

 

Variable Load Challenges:

 

Normal Operation:

 

  • Steady-state Claus tail gas - Consistent H₂S concentration (typically 0.5-2%)
  • Predictable flow - Relatively stable
  • Minimal fuel required

 

Upset Conditions:

 

  • Claus unit upsets - H₂S concentration spikes (can reach 10-30% or higher)
  • Start-up/shutdown - Variable composition and flow
  • Catalyst poisoning - Increased sulphur slip through Claus beds
  • Process unit upsets - Feed gas composition changes

 

How CRA Systems Handle Variability:

 

1. Combustion System Design:

 

  • Wide turndown burners (10:1 or greater)
  • Modulating fuel control responds to heat input changes
  • Auto-ignition capability for high H₂S loads
  • Flame stability across full operating range

 

2. High-Integrity Refractory:

 

  • Thermal shock resistant materials
  • Anchoring systems prevent spalling during thermal cycling
  • Multi-layer design - Hot face, insulating, backup layers
  • Expansion joints accommodate temperature variations

 

3. Temperature Control:

 

  • Automatic modulation maintains set point during load swings
  • Heat release monitoring adjusts for varying H₂S heating value
  • Override controls prevent over-temperature

 

4. Oxygen Control:

 

  • Trim air maintains excess oxygen set point
  • Monitors combustion efficiency
  • Prevents fuel-rich or oxygen-starved conditions

 

5. Safety Systems:

 

  • High-temperature shutdown protects refractory
  • Flame monitoring with auto-relight
  • Low-oxygen alarms for combustion safety
  • Bypass capability for emergency situations

What destruction efficiency can sulphur tail gas thermal oxidizers achieve?

Properly engineered systems typically achieve greater than 99.99% destruction efficiency for reduced sulphur compounds while maintaining stable performance across variable operating conditions.

 

Performance Standards:

 

  • H₂S destruction: >99.99%
  • COS and CS₂ destruction: >99.9%
  • Overall sulphur recovery: Often >99.5-99.9% when integrated with Claus unit
  • SO₂ emissions: Typically <250 ppm (or lower per local regulations)

 

Reactions in Thermal Oxidizer:

 

  • H₂S + 3/2 O₂ → SO₂ + H₂O
  • COS + 3/2 O₂ → SO₂ + CO₂
  • CS₂ + 3 O₂ → 2SO₂ + CO₂
  • Mercaptans + O₂ → SO₂ + H₂O + CO₂

 

Ensuring High DRE:

 

  • Temperature control: 650-1,480°C depending on sulphur load
  • Residence time: Minimum 1-2 seconds
  • Excess oxygen: Sufficient for complete oxidation
  • Burner design: Even temperature distribution
  • Continuous monitoring: SO₂, O₂, CO verification

What operating parameters are critical for sulphur tail gas thermal oxidizer performance?

Several interconnected parameters directly influence performance:

 

1. Operating Temperature:

 

  • Range: Typically about 650-1,480°C (1,200-2,700°F) depending on sulphur loading
  • Normal Claus tail gas: 950-1,050°C (1,740-1,920°F)
  • High H₂S upsets: May reach 1,200-1,480°C (2,190-2,700°F) auto-thermally
  • Control philosophy: Balance between complete destruction and refractory protection

 

2. Residence Time:

 

  • Typical: 1-2 seconds minimum at oxidation temperature
  • Purpose: Complete conversion of all sulphur species to SO₂
  • Design: Chamber volume sized for worst-case flow

 

3. Combustion Air Control:

 

  • Excess oxygen: 2-5% in stack
  • Stoichiometry: Sufficient for complete oxidation
  • Trim control: Automated adjustment based on O₂ measurement

 

4. Refractory Selection:

 

  • Hot face: High-alumina castable (for thermal/chemical resistance)
  • Insulation: Lightweight insulating firebrick or ceramic fiber
  • Thickness: Typically 200-450mm (8-18 inches) total
  • Anchors: Stainless steel or Inconel for longevity

 

5. Corrosion-Resistant Materials:

 

  • Shell: Carbon steel with refractory lining
  • Ductwork: 316 stainless steel minimum (SO₂/SO₃ environment)
  • Stack: Acid-resistant materials (FRP, exotic alloys, or brick-lined)
  • Instruments: Wetted parts in Hastelloy or Teflon-coated

 

6. Downstream Treatment (If Required):

 

  • SO₂ scrubbing with caustic or lime if emission limits require
  • Selective catalytic reduction (SCR) for NOx control if needed
  • Stack gas reheat to prevent visible plume

 

7. Monitoring and Controls:

 

  • Temperature profiling - Multiple zones
  • O₂ and SO₂ analyzers in stack
  • Pressure differential monitoring
  • Refractory temperature thermocouples
  • Safety interlocks and automated controls

 

Critical for: Consistent oxidation of all reduced sulphur species, Equipment longevity in corrosive sulphur service, Long-term reliability during variable SRU operation, and Regulatory compliance for SO₂, NOx, and particulate emissions.

 

CRA's 30+ Years of Sulphur Service Experience: CRA delivers oxidizers built specifically for extreme sulphur service with proven refractory designs, corrosion-resistant materials, and advanced controls that ensure reliable performance year after year.

Are these FAQ answers guaranteed for my specific application?

No. The information in these FAQs is for general guidance only. Every application is unique, and actual performance depends on your specific process conditions, site requirements, and operating parameters. Detailed engineering analysis of your process data is required to provide accurate specifications and performance guarantees. Contact CRA's engineering team for a comprehensive proposal tailored to your specific needs.

Custom engineered. Properly scoped.

Speak to an engineer