Catalytic non-thermal plasma reactor for oxidative degradation of toluene present in low concentration

被引:8
作者
Bhargavi, K. V. S. S. [1 ]
Ray, Debjyoti [1 ]
Chawdhury, Piu [1 ]
Rajanikanth, B. S. [2 ]
Thatikonda, Shashidhar [3 ]
Challapalli, Subrahmanyam [1 ]
机构
[1] Indian Inst Technol Hyderabad, Dept Chem, Hyderabad 502285, Telangana, India
[2] Indian Inst Sci, Dept Elect Engn, Bengaluru 560012, Karnataka, India
[3] Indian Inst Technol Hyderabad, Dept Civil Engn, Hyderabad 502285, Telangana, India
关键词
Non-thermal plasma; Plasma catalysis; VOC degradation; DBD reactor; VOLATILE ORGANIC-COMPOUNDS; ASSISTED CATALYSIS; FLOW-RATE; PART; DISCHARGE; DECOMPOSITION; ABATEMENT; AIR; DESTRUCTION; PERFORMANCE;
D O I
10.1016/j.cattod.2023.01.005
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
Toluene is a common solvent used in paints, pesticides, resins, etc. Although toluene is found in low concentrations in an indoor environment, long-term exposure to it is hazardous. This research aims to study toluene oxidation in a catalyst-packed dielectric barrier discharge (DBD) reactor designed to withstand high flow rates. The DBD reactor was packed with commercially available Al2O3 first and then with Mn and Co oxide-coated Al2O3. The surface modification of Al2O3 with transition metal oxides significantly improved the reactor's performance. At a power input of 20.3 W (equivalent to 13.0 J/l), MnO2/Al2O3 efficiently decomposed 50 ppm toluene (93%), and the corresponding CO2 selectivity was 57%. The in-situ breakdown of ozone, which leads to the formation of more reactive oxidants such as atomic oxygen, appears to make MnO2/Al2O3 better among the catalysts studied. The mean electron energies and the energy electron distribution function were calculated using the BOLSIG+ program.
引用
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页数:11
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