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
相关论文
共 38 条
[1]   The influence of zeolite acidity for the coupled hydrogenation and ring opening of 1-methylnaphthalene on Pt/USY catalysts [J].
Arribas, MA ;
Martínez, A .
APPLIED CATALYSIS A-GENERAL, 2002, 230 (1-2) :203-217
[2]   Scale-up analysis and development of gliding arc discharge facility for volatile organic compounds decomposition [J].
Bo, Zheng ;
Yan, Jianhua ;
Li, Xiaodong ;
Chi, Yong ;
Cen, Kefa .
JOURNAL OF HAZARDOUS MATERIALS, 2008, 155 (03) :494-501
[3]   Kinetic modeling for assessing the product distribution in toluene hydrocracking on a Pt/HZSM-5 catalyst [J].
Castano, Pedro ;
Arandes, Jose Maria ;
Pawelec, Barbara ;
Azar, Martin ;
Bilbao, Javier .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (04) :1043-1050
[4]   Decomposition of benzene as a surrogate tar in a gliding Arc plasma [J].
Chun, Young Nam ;
Kim, Seong Cheon ;
Yoshikawa, Kunio .
ENVIRONMENTAL PROGRESS & SUSTAINABLE ENERGY, 2013, 32 (03) :837-845
[5]   Toluene and butyl acetate removal from air by plasma-catalytic system [J].
Demidiouk, V ;
Moon, SI ;
Chae, JO .
CATALYSIS COMMUNICATIONS, 2003, 4 (02) :51-56
[6]   Pretreated olivine as tar removal catalyst for biomass gasifiers: investigation using naphthalene as model biomass tar [J].
Devi, L ;
Ptasinski, KJ ;
Janssen, FJJG .
FUEL PROCESSING TECHNOLOGY, 2005, 86 (06) :707-730
[7]   Pyrolysis products from different biomasses: application to the thermal cracking of tar [J].
Fagbemi, L ;
Khezami, L ;
Capart, R .
APPLIED ENERGY, 2001, 69 (04) :293-306
[8]   Catalytic Decomposition of Biomass Tars with Dolomites [J].
Gusta, Elizabeth ;
Dalai, Ajay K. ;
Uddin, Azhar ;
Sasaoka, Eiji .
ENERGY & FUELS, 2009, 23 (3-4) :2264-2272
[9]   Microwave plasma application in decomposition and steam reforming of model tar compounds [J].
Jamroz, P. ;
Kordylewski, W. ;
Wnukowski, M. .
FUEL PROCESSING TECHNOLOGY, 2018, 169 :1-14
[10]   Influence of supports on catalytic behavior of nickel catalysts in carbon dioxide reforming of toluene as a model compound of tar from biomass gasification [J].
Kong, Meng ;
Fei, Jinhua ;
Wang, Shuai ;
Lu, Wen ;
Zheng, Xiaoming .
BIORESOURCE TECHNOLOGY, 2011, 102 (02) :2004-2008