Adsorption Followed by Plasma Assisted Catalytic Conversion of Toluene into CO2 on Hopcalite in an Air Stream

被引:4
|
作者
Sonar, Shilpa [1 ,2 ]
Giraudon, Jean-Marc [1 ]
Veerapandian, Savita Kaliya Perumal [2 ]
Lamonier, Jean-Francois [1 ]
Morent, Rino [2 ]
Lofberg, Axel [1 ]
De Geyter, Nathalie [2 ]
机构
[1] Univ Artois, Cent Lille, Univ Lille, UMR 8181,Unite Catalyse & Chim Solide, F-59000 Lille, France
[2] Univ Ghent, Fac Engn & Architecture, Dept Appl Phys, Res Unit Plasma Technol, St Pietersnieuw Str 41 B4, B-9000 Ghent, Belgium
关键词
adsorption; adsorption plasma catalysis; hopcalite; non-thermal plasma; toluene removal; MANGANESE OXIDES; TOTAL OXIDATION; REMOVAL; VOCS; ABATEMENT; DECOMPOSITION; FORMALDEHYDE; PERFORMANCE; SYSTEM; AG;
D O I
10.3390/catal11070845
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The abatement of toluene was studied in a sequential adsorption-plasma catalysis (APC) process. Within this process, Hopcalite was used as bifunctional material: as adsorbent (storage stage) and as catalyst via the oxidation of adsorbed toluene (discharge stage). It was observed that the desorption and oxidation activity of the adsorbed toluene was significantly affected the process variables. In addition, the adsorption time influenced the CO2 selectivity and CO2 yield by changing the interaction between the catalyst and the plasma generated species. At least four APC sequences were performed for each examined condition suggesting that Hopcalite is very stable under plasma exposure during all the sequences. Consequently, these results could contribute to advance the plasma-catalyst system with an optimal VOC oxidation efficiency. The catalytic activity, amount of toluene adsorbed, amount of toluene desorbed and product formation have been quantified by FT-IR. Moreover, the catalyst was characterized by XRD, H-2-TPR, N-2 adsorption-desorption analysis and XPS. Hopcalite shows a good CO2 selectivity and CO2 yield when the APC process is performed with an adsorption time of 20 min and a plasma treatment with a discharge power of 46 W which leads to a low energy cost of 11.6 kWh center dot m(-3) and energy yields of toluene and CO2 of 0.18 (+/- 0.01) g center dot kWh(-1) and 0.48 (+/- 0.06) g center dot kWh(-1) respectively.
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页数:18
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