Our main clientele includes: industrial waste gas treatment companies, ozone purification equipment manufacturers, environmental protection companies in the motor vehicle, shipbuilding, exhaust gas treatment, petrochemical, and chemical industries, coating, printing, VOCs treatment, municipal and industrial wastewater treatment companies, flue gas treatment companies in the metallurgical and thermal power industries, laboratory and enclosed space air purification equipment manufacturers, and environmental engineering general contracting and operation and maintenance companies.
Degradation Due to Catalyst Poisoning Industrial-grade ozone decomposition catalysts use manganese dioxide and copper oxide as core active components. The key to their catalytic decomposition of ozone lies in the active sites on the surface. Ozone molecules complete the decomposition reaction by adsorbing onto the active sites. When poisoning occurs, toxic substances firmly occupy the active sites and cannot desorb. They also alter the valence state of active metals such as manganese and copper, directly resulting in the loss of catalytic activity. Some toxic substances can also clog catalyst pores, preventing ozone molecules from contacting the internal active sites, ultimately leading to a precipitous drop in catalytic efficiency, manifested as rapid catalyst degradation.
in Industrial Scenarios Various impurities in industrial environments can poison ozone decomposition catalysts. In order of toxicity, the most significant toxicity comes from sulfides (H₂S, SO₂), which are highly poisonous to ozone catalysts; even trace amounts can cause rapid poisoning. Next are halogens/chlorine-containing substances (HCl, Cl₂), heavy metals such as arsenic, lead, and mercury. Furthermore, high-boiling-point VOCs, carbon deposits from industrial oil pollution, and salt crystals precipitated under high humidity conditions can also gradually poison the catalyst, leading to degradation.
A water treatment company, in its ozone oxidation tailwater quality control, used a conventional ozone decomposition catalyst. Due to the presence of trace amounts of sulfides in the tailwater and the lack of pretreatment, the catalyst's ozone decomposition efficiency plummeted from 98% to 45% after only one month of use, exhibiting severe degradation. After optimizing the pretreatment process for sulfides and replacing it with a more toxic manganese dioxide-copper oxide-based ozone decomposition catalyst, the catalytic efficiency stabilized above 95% and showed no significant degradation even after two years of continuous use, greatly reducing the frequency of catalyst replacement.
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