Thermal oxidisers (also called incinerators or thermox) destroy VOCs, HAPs and odorous compounds by raising the contaminated air to combustion temperature (760–1100°C, residence time 0.5–1 second), breaking hydrocarbon bonds down to CO2 and water vapour. Destruction efficiency 95–99.9% depending on duty.
Choose thermal oxidation when:
Choose against thermal oxidation when:
Direct-fired oxidiser — simplest design, single combustion chamber, no heat recovery. Lowest capital cost, highest fuel burn. 760–870°C typical. Best for streams with high VOC concentrations where the VOCs contribute to combustion fuel.
Recuperative oxidiser — adds an air-to-air heat exchanger to preheat inlet air with the hot exhaust. 60–70% thermal recovery. Lower fuel cost than direct-fired, larger footprint. Good for moderate VOC streams.
Regenerative thermal oxidiser (RTO) — ceramic heat-sink beds switch between heating and cooling cycles. 90–95% thermal recovery. Highest capital cost, lowest operating cost — the dominant choice for industrial paint booths, printing, chemical reactor vents and pharma fermenters. 815–980°C operating.
Catalytic oxidiser (CatOx) — Pt or Pd catalyst on a honeycomb support lowers the operating temperature to 320–450°C. Sharply lower fuel use vs thermal, but catalyst is poisoned by halogens, heavy metals, sulphur and silicones. Best suited to clean VOC streams from well-characterised processes.
Common applications: paint booths, printing presses, chemical reactor vents, pharma fermenter vents, semiconductor abatement, food processing odour control.
Design limits to engineer against: NOx generation at high temp (especially RTO), acid gases from halogenated VOCs (HCl, HF, HBr — require downstream scrubbing), catalyst poisoning on CatOx. We size the package against your VOC composition, target destruction efficiency, available utilities (natural gas, LPG, process fuel), and licence-driven outlet limits.
Need more information? Contact our team for more specialised advice.