甲苯
苯
催化作用
大气压力
非热等离子体
等离子体
化学
填充床
化学工程
分析化学(期刊)
色谱法
有机化学
气象学
物理
量子力学
工程类
作者
Alice M. Harling,Hyun‐Ha Kim,Shigeru Futamura,J. Christopher Whitehead
摘要
A nonthermal, atmospheric pressure, packed-bed plasma reactor has been used to study the effect of temperature on the plasma−catalytic destruction of toluene and benzene in air. The plasma reactor was packed with BaTiO3 beads to which TiO2, γ-Al2O3, and Ag, Pt, or Pd impregnated catalysts were added. The reactor can be heated up to ∼500 °C, and the destruction efficiencies for toluene and benzene were determined for plasma alone, catalyst alone, and the combined plasma−catalyst configuration. Comparisons have been made to determine the relative contributions of the catalyst and plasma and to discover any synergistic effects. Plasma−catalysis shows greater destruction than catalysis alone with increasing temperature for both benzene and toluene. Catalysis alone has a threshold temperature of ∼300 °C for the destruction of toluene and benzene, but plasma−catalysis with Pd- and Pt-impregnated alumina achieves >95% destruction at this temperature and has a threshold of ∼100 °C. Toluene is more easily destroyed than benzene at all temperatures, by all catalysts.
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