Removal of Toluene as a Biomass Tar Surrogate in a Catalytic Nonthermal Plasma Process | |
Xu, Bin1,2; Xie, Jianjun1; Zhan, Hao1,2; Yin, Xiuli1; Wu, Chuangzhi1; Liu, Hao3 | |
刊名 | ENERGY & FUELS
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2018-10-01 | |
卷号 | 32期号:10页码:10709-10719 |
ISSN号 | 0887-0624 |
DOI | 10.1021/acs.energyfuels.8b02444 |
通讯作者 | Xie, Jianjun(xiejj@ms.giec.ac.cn) |
英文摘要 | In this study, a packed-bed dielectric barrier discharge (DBD) reactor was developed to investigate the removal of biomass tar in a fuel gas atmosphere. Toluene was used as the tar surrogate, and the catalyst used was a Nickel-based catalyst (Ni/gamma-Al2O3) because of its high activity and low cost. In addition, another two kinds of packing materials (glass pellets and gamma-Al2O3 pellets) were employed to make a comparison with the Ni/gamma-Al2O3 catalyst. The research has focused on the removal efficiency of toluene and the effects of carrier gas, reaction temperature, Ni loading, and concentration of toluene. The results indicated that two supplementary packing materials could not realize an effective removal of toluene. On the contrary, Ni/gamma-Al2O3 combined with plasma showed a significant synergetic effect and hence a great toluene removal potential. On one hand, the removal efficiency initially decreased within the temperature range of 200-300 degrees C and then significantly increased within the temperature of 300-400 degrees C during plasma-catalytic process. At the optimal temperature of 400 degrees C, the toluene removal efficiency could reach the maximum values of 80.2%, 91.7%, and 100.0% when the Ni loading was 3, 5, and 10 wt %, respectively. On the other hand, an increase in the inlet toluene concentration slightly reduced removal-efficiency but increased the energy efficiency, reaching the highest value of 16.8 g/kWh. The introduction of plasma enhanced the methanation reaction of the fuel gas occurring in the catalytic process, which was favorable at high temperatures. Based on these findings, the mechanisms and pathways of toluene destruction in the plasma-catalytic process were proposed and elucidated. |
资助项目 | National Natural Science Foundation of China[51576200] ; National Natural Science Foundation of China[51811530317] ; Natural Science Foundation of Guangdong Province of China[2017B030308002] ; Royal Society International Exchanges 2017 Cost Share (China)[IEC\NSFC\170654] |
WOS关键词 | DIELECTRIC BARRIER DISCHARGE ; PULSED CORONA DISCHARGES ; SYNTHETIC NATURAL-GAS ; GLIDING ARC-DISCHARGE ; MODEL-COMPOUND ; SYNGAS METHANATION ; NI/AL2O3 CATALYSTS ; PRODUCER GAS ; BIO-SYNGAS ; PACKED-BED |
WOS研究方向 | Energy & Fuels ; Engineering |
语种 | 英语 |
出版者 | AMER CHEMICAL SOC |
WOS记录号 | WOS:000448087000067 |
资助机构 | National Natural Science Foundation of China ; Natural Science Foundation of Guangdong Province of China ; Royal Society International Exchanges 2017 Cost Share (China) |
内容类型 | 期刊论文 |
源URL | [http://ir.giec.ac.cn/handle/344007/24143] ![]() |
专题 | 中国科学院广州能源研究所 |
通讯作者 | Xie, Jianjun |
作者单位 | 1.Chinese Acad Sci, Guangzhou Inst Energy Convers, CAS Key Lab Renewable Energy, Guangdong Prov Key Lab New & Renewable Energy Res, Guangzhou 510640, Guangdong, Peoples R China 2.Univ Chinese Acad Sci, Beijing 100049, Peoples R China 3.Univ Nottingham, Fac Engn, Dept Architecture & Built Environm, Univ Pk, Nottingham NG7 2RD, England |
推荐引用方式 GB/T 7714 | Xu, Bin,Xie, Jianjun,Zhan, Hao,et al. Removal of Toluene as a Biomass Tar Surrogate in a Catalytic Nonthermal Plasma Process[J]. ENERGY & FUELS,2018,32(10):10709-10719. |
APA | Xu, Bin,Xie, Jianjun,Zhan, Hao,Yin, Xiuli,Wu, Chuangzhi,&Liu, Hao.(2018).Removal of Toluene as a Biomass Tar Surrogate in a Catalytic Nonthermal Plasma Process.ENERGY & FUELS,32(10),10709-10719. |
MLA | Xu, Bin,et al."Removal of Toluene as a Biomass Tar Surrogate in a Catalytic Nonthermal Plasma Process".ENERGY & FUELS 32.10(2018):10709-10719. |
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