Upgrading of lignin-derived bio-oil in non-catalytic plasma reactor: Effects of operating parameters on 4-methylanisole conversion

被引:30
作者
Hosseinzadeh, Mohammad Bagher [1 ]
Rezazadeh, Shahin [1 ]
Rahimpour, Hunk Reza [1 ]
Taghvaei, Hamed [1 ]
Rahimpour, Mohammad Reza [1 ,2 ]
机构
[1] Shiraz Univ, Sch Chem & Petr Engn, Dept Chem Engn, Shiraz 71345, Iran
[2] Univ Calif Davis, Dept Chem Engn & Mat Sci, Davis, CA 95616 USA
关键词
Biomass; Bio-oil; 4-Methylanisole; Upgrading; Non-thermal plasma; FAST PYROLYSIS; NONTHERMAL PLASMA; CATALYTIC CONVERSION; REACTION NETWORK; CARRIER GAS; DISCHARGE; CRACKING; ANISOLE; VOLTAGE; HYDRODEOXYGENATION;
D O I
10.1016/j.cherd.2015.08.017
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This article investigated an atmospheric pressure dielectric barrier discharge (DBD) plasma reactor to explore the effects of carrier gas type, applied voltage and pulse repetition frequency on upgrading of 4-methylanisole as a lignin-derived bio-oil. A series of experiments were designed to realize the effects of argon (Ar) and hydrogen (H-2) on upgrading. The results showed that argon yields higher conversion of 4-methylanisole compared to hydrogen, and both voltage and frequency had positive effects on the conversion of 4-methylanisole. Increasing voltage and frequency led to an increase in the number of active species and subsequently, the number of effective collisions as a result 4-methylanisole conversion and discharge power (DP). In the experiments with applied voltage of 9 kV, frequency of 20 kHz and existence of Ar as carrier gas, the conversion reached to 29.80% at the DP of 77 W. The most abundant products were 4-methyphenol and 2,4-dimethylphenol, which were formed from transalkylation and hydrogenolysis reactions. It was found that the increase in the applied voltage, frequency and Ar percentage of carrier gas (as adjustable parameters), has the same effects on product distribution; since their variation resulted in the same changes in core plasma parameters such as electron energy, temperature and density. (C) 2015 The Institution of Chemical Engineers. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:296 / 305
页数:10
相关论文
共 51 条
[31]   Effect of filter media size, mass flow rate and filtration stage number in a moving-bed granular filter on the yield and properties of bio-oil from fast pyrolysis of biomass [J].
Paenpong, Chaturong ;
Inthidech, Sudsakorn ;
Pattiya, Adisak .
BIORESOURCE TECHNOLOGY, 2013, 139 :34-42
[32]  
Park HJ, 2006, STUD SURF SCI CATAL, V159, P553
[33]  
Pham T.N., 2013, APPL CATAL B
[34]   Bio-oil hydrodeoxygenation: Adsorption of phenolic compounds on sulfided (Co)Mo catalysts [J].
Popov, Andrey ;
Kondratieva, Elena ;
Mariey, Laurence ;
Goupil, Jean Michel ;
El Fallah, Jaafar ;
Gilson, Jean-Pierre ;
Travert, Arnaud ;
Mauge, Francoise .
JOURNAL OF CATALYSIS, 2013, 297 :176-186
[35]   Combination of non-thermal plasma and heterogeneous catalysis for methane and hexadecane co-cracking: Effect of voltage and catalyst configuration [J].
Rahimpour, M. R. ;
Jahanmiri, A. ;
Shirazi, M. Mohamadzadeh ;
Hooshmand, N. ;
Taghvaei, H. .
CHEMICAL ENGINEERING JOURNAL, 2013, 219 :245-253
[36]   Upgrading of Anisole in a Catalytic Pulsed Dielectric Barrier Discharge Plasma Reactor [J].
Rahimpour, Mohammad Reza ;
Jahanmiri, Abdolhossein ;
Rostami, Parisa ;
Taghvaei, Hamed ;
Gates, Bruce C. .
ENERGY & FUELS, 2013, 27 (12) :7424-7431
[37]  
Runnebaum R. C., 2011, CATAL LETT, V142, P7
[38]   Catalytic conversion of compounds representative of lignin-derived bio-oils: a reaction network for guaiacol, anisole, 4-methylanisole, and cyclohexanone conversion catalysed by Pt/γ-Al2O3 [J].
Runnebaum, Ron C. ;
Nimmanwudipong, Tarit ;
Block, David E. ;
Gates, Bruce C. .
CATALYSIS SCIENCE & TECHNOLOGY, 2012, 2 (01) :113-118
[39]   UPGRADING OF WOOD-DERIVED BIO-OIL OVER HZSM-5 [J].
SHARMA, RK ;
BAKHSHI, NN .
BIORESOURCE TECHNOLOGY, 1991, 35 (01) :57-66
[40]   CATALYTIC UPGRADING OF PYROLYSIS OIL [J].
SHARMA, RK ;
BAKHSHI, NN .
ENERGY & FUELS, 1993, 7 (02) :306-314