Upgrading of Anisole in a Catalytic Pulsed Dielectric Barrier Discharge Plasma Reactor

被引:24
作者
Rahimpour, Mohammad Reza [1 ,2 ]
Jahanmiri, Abdolhossein [1 ]
Rostami, Parisa [1 ]
Taghvaei, Hamed [1 ]
Gates, Bruce C. [2 ]
机构
[1] Shiraz Univ, Sch Chem & Petr Engn, Dept Chem Engn, Shiraz 71345, Fars, Iran
[2] Univ Calif Davis, Dept Chem Engn & Mat Sci, Davis, CA 95616 USA
关键词
BIOMASS PYROLYSIS OIL; NONTHERMAL PLASMA; HYDROGEN-PRODUCTION; BIO-OIL; HETEROGENEOUS CATALYSIS; OXYGENATE COMPONENTS; HZSM-5; ZEOLITE; LIQUID FUEL; CRACKING; METHANE;
D O I
10.1021/ef401357f
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
A new strategy for bio-oils upgrading with a catalytic pulsed dielectric barrier discharge (DBD) plasma reactor was investigated for the conversion of anisole, a compound representative of the bio-oils formed by pyrolysis of lignin. The anisole conversion was measured with plasma alone and also in the presence of Al2O3 and various Al2O3-supported catalysts, leading to the formation of benzene, phenol, 4-methylanisole, 2-methylanisole, 4-methylphenol, 2-methylphenol, 2,6-dimethylphenol, and cyclohexane. Results are presented in the form of specific input energy (SIE), anisole conversion, and product selectivities. The conversion decreased in the following order when these catalysts were used: Mo-Ni/Al2O3 > Pt/Al2O3 > Co-Mo/Al2O3 > Pt-Re/Al2O3 > Al2O3. The conversion increased with increasing mass of the Mo-Ni/Al2O3 catalyst and with increasing voltage; the highest anisole conversion (0.81) was observed with this catalyst, and the conversion under comparable conditions without a catalyst was 0.43. The predominant product was 4-methylanisole. Catalyst deactivation was minimized by the plasma.
引用
收藏
页码:7424 / 7431
页数:8
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