Catalytic non-thermal plasma reactor for abatement of toluene

被引:97
|
作者
Subrahmanyam, Ch. [1 ]
Renken, A. [2 ]
Kiwi-Minsker, L. [2 ]
机构
[1] Indian Inst Technol, Dept Chem, Hyderabad 502205, Andhra Pradesh, India
[2] Swiss Fed Inst Technol, Dept Catalyt React Engn GGRC EPFL, CH-1015 Lausanne, Switzerland
关键词
Non-thermal plasma reactor; Dielectric barrier discharge; Oxidation of toluene; Ozone; VOLATILE ORGANIC-COMPOUNDS; ENVIRONMENTAL-POLLUTANTS; HETEROGENEOUS CATALYSIS; BENZENE DECOMPOSITION; DRIVEN CATALYST; AIR-POLLUTANTS; PART; OXIDATION; SYSTEM; COMBINATION;
D O I
10.1016/j.cej.2010.04.011
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
A non-thermal plasma rector with a catalytic electrode made of sintered metal fibres (SMFs) was tested for the oxidative decomposition of a model VOC toluene. The input energy was varied in the range 160-295 J/I by varying the applied voltage between 12.5 and 22.5 kV at 200 Hz. Influence of various parameters like toluene concentration, SMF modification by Mn and Co oxides, input energy and ozone formation was studied. It has been observed that plasma catalytic approach is very effective for total oxidation of toluene at low input energy, especially at toluene concentration <= 250 ppm and SMF modification by transition metal oxides increased the performance of the reactor significantly. MnO(x) modification appears to be a better choice compared to CoO(x), which may be attributed to the in situ decomposition of ozone leading to the formation of more reactive oxidants like atomic oxygen. (c) 2010 Elsevier B.V. All rights reserved.
引用
收藏
页码:677 / 682
页数:6
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