The coating industry is one of the major sources of industrial VOCs emissions. During the coating processes of automobiles, furniture, machinery, etc., organic solvents (toluene, xylene, ethyl acetate, etc.) in paints volatilize in large amounts during spraying and drying. Spray exhaust is characterized by low concentration (100–200 mg/m³), high air volume (hundreds of thousands of m³/h), ambient temperature, high humidity, and containing paint mist. Drying exhaust has a higher concentration (1,000–3,000 mg/m³).
On the policy front, national and local standards are becoming increasingly stringent. The Emission Standard for VOCs from Industrial Coating Processes requires that exhaust from solvent‑based coating operations be collected in enclosed spaces and treated before discharge. VOCs have been included in the scope of environmental protection tax, and excessive emissions will face higher tax rates and environmental credit deductions. For coating enterprises, VOCs treatment is a mandatory requirement for stable and compliant operation.
Catalytic combustion is the mainstream technology for coating VOCs treatment. Its principle is to oxidize VOCs into CO₂ and H₂O at a low temperature (200–400°C) under the action of a catalyst, avoiding NOₓ formation that occurs in direct high‑temperature combustion. The reaction equation is:
CₙHₘ + (n + m/4)O₂ → nCO₂ + (m/2)H₂O
Coating exhaust has high air volume and low concentration, making single‑stage catalytic combustion difficult to handle directly and efficiently. The industry commonly adopts the “dry filtration + adsorption concentration + catalytic combustion” combined process: exhaust first passes through three‑stage filtration to remove paint mist, then is concentrated 10–20 times by a zeolite rotor or activated carbon bed, and the high‑concentration gas enters the catalytic combustion chamber for decomposition. The released heat is used for desorption regeneration, achieving thermal energy recycling. This combined process balances treatment efficiency and operating economy.
Catalyst selection directly affects system efficiency and service life. It is recommended to follow the four steps below.
If the exhaust mainly contains benzene series and alcohols and contains no sulfur, chlorine, or silicon, a noble metal catalyst can be selected to ensure high purification efficiency. If it contains sulfur, chlorine, or organosilicon, a transition metal oxide catalyst with strong poison resistance must be used, or the poisons must be thoroughly removed in the pretreatment stage.
Monolithic honeycomb catalysts are widely adopted due to low bed pressure drop and easy handling. Catalyst cost accounts for 20%–30% of total equipment investment. Although high‑quality catalysts have a slightly higher initial purchase price, they have a service life of 2–3 years, making them more economical in the long term. For customized selection advice, please contact our technical team.
Scientific maintenance is the guarantee for long‑term efficient operation of catalysts. It is recommended to establish a full‑lifecycle system of “daily inspection – quarterly cleaning – annual testing”.
Check the filter cotton daily and replace it when resistance increases by 50%. Drain condensate weekly to prevent backflow. For severe paint mist, install three‑stage filtration (G4 coarse + F7 medium + high‑efficiency paint mist filter), which can remove more than 90% of paint mist particles.
Every 3 months, use compressed air to blow off dust from the catalyst surface in the direction of gas flow. If carbon deposits are found, wash with low‑pressure steam (120°C). Calculate the purification efficiency daily from inlet and outlet concentrations (normal ≥95%); if efficiency drops suddenly by more than 10%, shut down and inspect for poisoning or carbon deposition. Annually commission a third party to test catalyst activity.
Temporary deactivation caused by carbon deposition can be regenerated online: disconnect the exhaust inlet and gradually raise the catalyst bed temperature to 500–600°C for 2–4 hours to oxidize the carbonaceous matter.
The temperature fluctuation in the combustion chamber should be controlled within ±15°C. Strictly follow the “preheat before admitting gas” procedure to avoid cold gas directly impacting the hot catalyst bed.
Catalysts generally require complete replacement every 2–3 years, based on three criteria: activity loss >50%, breakage rate >15%, or exceeding the designed service life. Spent catalysts are hazardous waste and must be disposed of by qualified professional units; random dumping is strictly prohibited.
In coating industry VOCs treatment, catalyst selection and maintenance are equally important. Enterprises should accurately match the catalyst type according to exhaust characteristics and establish a full‑lifecycle maintenance system of “daily inspection – quarterly cleaning – annual testing”, enabling the catalyst to operate stably for more than 2 years and reducing overall costs by 25%–40%. If you need selection consultation or technical solution support, please contact our technical team for customized recommendations based on your actual operating conditions.
author:Gloria
date:2026-05-26
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