低温等离子体-催化联合技术去除甲苯的实验研究

    Removal of Toluene by Non-thermal Plasma Coupled With Catalyst

    • 摘要: 以挥发性有机污染物(volatile organic compounds,VOCs)代表物质甲苯为去除对象,采用低温等离子体-催化联合技术对其降解开展研究.比较了3种催化剂(TiO2、BaTiO3、TiO2+BaTiO3)等离子体反应器及无催化剂(空管)反应器对甲苯降解性能的异同;考察了BaTiO3和TiO2不同质量比下混合催化剂对甲苯的降解效果,确定了2种材料的最佳配比;对比了不同等离子体反应器的能耗;对生成的反应产物进行了测定分析.结果表明:有催化剂反应器对甲苯的降解性能均优于无催化剂反应器;不同类型催化剂反应器对甲苯的降解性能高低依次为:TiO2+BaTiO3—BaTiO3—TiO2;BaTiO3和TiO2质量比为2.375∶1的等离子体反应器对甲苯的去除效果最好,降解率最高达75.2%,且能耗相比其他催化剂最低,20 kV时功率为138.8 W.

       

      Abstract: Non-thermal plasma coupled with catalysis was employed to remove the toluene that was a representative pollutant of volatile organic compounds (VOCs). The effect of plasma reactors with or without fillings on toluene removal was investigated. Three kinds of catalysts were as follows: the catalyst of separate load TiO2 , BaTiO3 , or the mixed catalyst TiO2 + BaTiO3. The effect of plasma reactors by adding the mixed catalyst of different BaTiO3 and TiO2 mass ratios were investigated, while the optimal ratio of the two materials was explored; the energy consumption of the plasma reactors by adding various catalysts were also studied; and the reaction product was analyzed. Results showed that the toluene degradation ability of different catalyst reactors was as follows: the mixed catalyst of TiO2 + BaTiO3- separate load of BaTiO3-separate load of TiO2 ; the plasma reactor by adding mixed catalyst of BaTiO3 and TiO2 mass ratio of 2. 375 : 1 had the best degradation effect of toluene, and the minimum energy consumption compared to other catalysts. The highest toluene degradation rate was 75.2% and the power was 138.8 W at 20 kV.

       

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