Thermal Oxidizer vs Enclosed Flare: Choosing the Right Solution for VOC and Waste-Gas Control

Updated:
December 29th, 2025
12
min
read

Thermal Oxidizer vs Enclosed Flare: Choosing the Right Solution for VOC and Waste-Gas Control

Bruno Moons
Updated:
November 12th, 2024
12 mins
read
Biogas
Biogas
In this Article
Introduction


Industrial emissions of VOCs, waste gases or odours are a major environmental and regulatory concern. Combustion-based systems are among the most widely adoptedmethods to convert these emissions into carbon dioxide and water. But one sizedoesn’t fit all. Thermal oxidizers are engineered for steady, controlledprocess exhausts; enclosed flares are built for flexibility across flow andcomposition extremes. Understanding how these systems differ is key tooptimizing capital cost, energy use and compliance performance.

What is a Thermal Oxidizer

A thermal oxidizers is a combustion system designed to treat a process exhaust stream containing VOCs or odours, ensuring high destruction removal efficiency (DRE) bymaintaining sufficient temperature, residence time and mixing. There areseveral variants:

  • Direct-fired (DFTO) — basic burner + chamber
  • Recuperative — adds heat-exchanger to recover     exhaust heat
  • Regenerative (RTO) — uses ceramic media to capture     and reuse heat

These systems aretypically sized for steady or moderately variable gas flows andconcentrations, allowing process integration, heat recovery and continuousduty. With proper design they achieve DREs ≥ 98-99 % and often much higher.

What Is an Enclosed Flare?

An enclosed flareis a combustion device in which a waste or relief gas is fed into arefractory-lined chamber or enclosure where it is burnt without a visibleexternal flame. Often used in oil & gas, landfill, biogas or petrochemicaloperations, enclosed flares are designed for variable flow, widecomposition range, and rapid change in load. They provide flameinvisibility (important for community/urban settings), lower radiant heatexposure, and flexible operation under upset or relief conditions.

Key Design & Operational Differences
Feature Thermal Oxidizer Enclosed Flare
Combustion Type Controlled burner and chamber with designed flow, temperature, and residence time Diffusion or assisted flame within an enclosed chamber; wide operating range
Temperature Range Typically ~760–1,100 °C (1,400–2,000 °F), depending on gas and design Often ~900–1,200 °C (1,650–2,200 °F) to ensure complete destruction and no visible flame
Flow / Load Suitability Best for steady to moderately variable flows and VOC concentrations Handles wide variation, from low to high flows, including relief and upset events
Heat Recovery Potential Yes, available in recuperative and regenerative (RTO) configurations Rarely applied; primarily designed for gas destruction rather than recovery
Complexity & Controls High — includes heat exchangers, fans, valves, and continuous monitoring Moderate to high — pilot systems, air or steam assist, and instrumentation
Energy / Fuel Use Lower with heat recovery; higher fuel use without recovery Generally higher fuel use per unit mass treated unless gas has high BTU content
Site & Community Impact No visible flame, but stack height, radiation, and noise must be managed Minimal visible flame and lower radiant heat, suitable for populated areas
Maintenance Requirements Higher due to system complexity, instrumentation, and possible media wear Robust design, with routine checks on blowers, pilots, and chamber lining

Performance & Efficiency

Thermal oxidizer can provide veryhigh, stable DREs when designed for specific process flows — especially whenheat recovery is integrated, reducing fuel consumption significantly.


Enclosed flares provide robustness and flexibility: while DRE is stillhigh if properly designed, the variable nature of gas composition, flow rateand assist requirements can make achieving optimal fuel-efficiency morechallenging. Because enclosed flares are often chosen for flexibility ratherthan optimized steady duty, their fuel cost per unit gas treated may be higherin continuous service.

Safety & Regulatory Aspects

Both technologiesmust satisfy stringent emission, safety and performance criteria:

  • Destruction removal efficiency (DRE)     targets (often ≥ 98-99 %)
  • Visible emission (plume) control
  • Stack gas monitoring (CO, O₂,     temperature)
  • Radiation, noise, and community impact     assessment

Enclosed flareshave a particular advantage when the site is near communities or when visibleflame must be minimized. Thermal oxidizers offer advantages where processexhausts are well-defined and continuous, allowing tighter control overemissions.

When to Use Each Technology

Use a ThermalOxidizer when:

  • VOC/odour exhaust is steady and     predictable
  • Continuous hours of operation justify     the investment and fuel savings
  • Emission limits are strict and heat     recovery is economically justified
  • Maintenance resources exist to support     more complex equipment

Use an EnclosedFlare when:

  • Gas flow or composition is highly     variable, including relief or emergency loads
  • You require minimal visible flame,     fewer public impact concerns, or odor control
  • Simplicity and rapid response are more     important than maximal fuel efficiency
  • You deal with waste- or relief-gas     streams rather than steady process exhausts

Example Applications
  • Pharmaceutical / chemical plant: A thermal oxidizer (recuperative or     regenerative type) is installed on a continuous solvent vent stream —     efficient, capable of heat recovery and designed for high uptime.
  • Biogas / landfill facility: An enclosed flare is selected to     combust variable-BTU landfill gas, ensure no visible flame for nearby     community, and handle intermittent spikes.
  • Refinery relief system: An enclosed flare accommodates large     relief volumes during upset scenarios, providing reliable destruction with     low visual footprint and robust safety margins.

Conclusion

Both thermaloxidizers and enclosed flares are powerful combustion-based abatementtechnologies, but their best-fit scenarios differ. Thermal oxidizers excel in steady,controlled process streams with potential for heat recovery and highefficiency. Enclosed flares excel in flexible, variable, high-load orrelief-gas scenarios, especially where visible flame, community impact orsimplicity are major concerns.

The right solutiondepends on your facility’s gas composition, flow variability, operationalhours, regulatory environment, and energy/fuel cost. A lifecyclecost and performance analysis (CAPEX + OPEX + fuel + maintenance + emissions)will guide you to the optimal choice.

Custom engineered. Properly scoped.

Speak to an engineer