Removal of Toluene as a Tar Analogue in a N2 Carrier Gas Using a Non-thermal Plasma Dielectric Barrier Discharge Reactor

被引:21
作者
Saleem, Faisal [1 ,2 ]
Zhang, Kui [1 ]
Harvey, Adam [1 ]
机构
[1] Newcastle Univ, Sch Engn, Newcastle Upon Tyne NE1 7RU, Tyne & Wear, England
[2] Univ Engn & Technol, Dept Chem & Polymer Engn, Faisalabad Campus, Faisalabad 38000, Punjab, Pakistan
基金
英国工程与自然科学研究理事会;
关键词
MODEL-COMPOUND; BIOMASS GASIFICATION; PYROLYSIS PRODUCTS; LOWER HYDROCARBONS; ENERGY-PRODUCTION; DECOMPOSITION; STEAM; HYDROCRACKING; DESTRUCTION; TEMPERATURE;
D O I
10.1021/acs.energyfuels.8b03618
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
The role of N-2 carrier gas toward the conversion of tar analogue (toluene) was studied in a non-thermal plasma dielectric barrier discharge reactor. The parameters investigated were power (5-40 W), residence time (1.43-4.23 s), toluene concentration (20-82 g/Nm(3)), and wall temperature (from ambient to 400 degrees C). Almost complete removal (99%) of toluene was observed at 40 W and 4.23 s. The main gaseous product was H-2, with a maximum selectivity of 40%. The other gaseous products were lighter hydrocarbons (LHCs, C-1-C-6, 5.5%). The selectivity to these LHCs could be increased to 10% by increasing the temperature to 400 degrees C. Introducing H-2 to the N-2 carrier gas at elevated temperatures opened up new reaction routes to enhance the selectivity to LHCs. The selectivity to methane reached 44% at 35% H-2 at 400 degrees C, and the total selectivity to LHCs reached 57%.
引用
收藏
页码:389 / 396
页数:8
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