

Temperature is one of the most important operating parameters affecting catalytic oxidation efficiency. Pollutant molecules typically undergo adsorption, surface activation, oxidation, and product desorption on the catalyst surface. When the temperature is too low, the reaction rate may be insufficient, limiting pollutant conversion.
Catalytic oxidation performance can be characterized using parameters such as T10, T50, and T90, which represent the temperatures corresponding to 10%, 50%, and 90% pollutant conversion, respectively. These indicators provide a practical way to evaluate the temperature-dependent activity of a catalyst. In industrial applications, however, a higher temperature is not necessarily better. Energy consumption, long-term catalyst stability, and the allowable operating temperature range of the equipment must also be considered.
The inlet pollutant concentration directly affects the pollutant load entering the catalyst bed. A change in concentration not only changes the amount of pollutant that must be treated per unit of time, but may also alter surface coverage and the reaction state of the catalyst.
If the actual pollutant concentration is significantly higher than the design condition, conversion performance may change even when temperature and gas flow remain constant. A higher concentration can also increase the reaction load and, for strongly exothermic oxidation reactions, affect the heat released within the catalyst bed. Therefore, process design should consider not only the average concentration but also the normal concentration, maximum concentration, and expected concentration fluctuations.
Gas flow rate determines the amount of gas passing through the catalyst bed per unit of time. In catalytic oxidation systems, gas hourly space velocity (GHSV) is commonly used to describe the relationship between gas throughput and catalyst volume:
GHSV = Gas volumetric flow rate ÷ Catalyst bed volume
When the catalyst volume remains constant, increasing the gas flow rate generally increases the GHSV and reduces the average residence time of the gas in the catalyst bed. If the reaction kinetics cannot support the increased treatment load, pollutant conversion may decrease.
Therefore, catalyst loading, gas flow rate, space velocity, and the required conversion level must be considered together. Space velocity should not be evaluated independently of temperature because the same GHSV can result in significantly different conversion performance at different reaction temperatures.
Catalytic oxidation requires an oxidizing agent, making oxygen concentration another important operating parameter. For some oxidation reactions, insufficient oxygen availability may limit pollutant conversion. However, increasing the oxygen concentration does not necessarily produce a proportional increase in catalytic oxidation efficiency for every catalyst-pollutant system.
This is because catalytic oxidation involves not only gas-phase transport but also adsorption and redox reactions on the catalyst surface. Different catalysts and pollutants have different oxygen requirements. Therefore, oxygen concentration should be evaluated together with the target pollutant, catalyst properties, and other operating conditions.
Industrial exhaust gases commonly contain water vapor and multiple coexisting components. Water vapor may compete with pollutants for adsorption sites on the catalyst surface and can alter surface hydroxyl species and reaction pathways, thereby affecting catalytic oxidation performance.
Other coexisting compounds can also influence catalyst behavior. For example, certain sulfur-containing compounds, halogenated compounds, or high concentrations of organic compounds may interact with or cover active sites, resulting in temporary inhibition or, under certain conditions, long-term catalyst deactivation. In multicomponent gas streams, competitive adsorption and competing reactions between different pollutants may also occur.
Therefore, catalyst evaluation should not be based only on the name and concentration of the target pollutant. The oxygen concentration, water vapor content, and concentration ranges of major coexisting impurities should also be identified whenever possible.
In real operating conditions, these parameters rarely change independently. For example, increasing the gas flow rate increases GHSV and generally shortens residence time; increasing pollutant concentration increases the reaction load; changes in humidity may affect pollutant adsorption on the catalyst surface; and changes in temperature directly affect the reaction rate. As a result, the same catalyst can show significantly different performance under different operating conditions.
When determining whether a catalytic oxidation process is suitable for a specific application, the assessment should include at least the pollutant type and concentration, peak concentration, gas flow rate, GHSV, operating temperature, oxygen concentration, humidity, and coexisting gas components. These parameters should then be evaluated together with catalyst activity, catalyst loading, and the required conversion level to establish a suitable operating window.
Overall, catalytic oxidation performance is not determined by a single operating parameter. It results from the combined effects of reaction kinetics, gas-solid contact conditions, and gas composition. In practical engineering, the objective is not simply to identify one “optimal parameter,” but to establish a stable operating range in which temperature, pollutant concentration, space velocity, and gas composition can collectively support the required conversion level.
author:kaka
date:2026/9/28
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