Production of renewable fuels by blending bio-oil with alcohols and upgrading under supercritical conditions

被引:29
作者
Omar, Sainab [1 ]
Alsamaq, Suzanne [1 ]
Yang, Yang [2 ]
Wang, Jiawei [1 ,2 ]
机构
[1] Aston Univ, Chem Engn & Appl Chem, Birmingham B4 7ET, W Midlands, England
[2] Aston Univ, European Bioenergy Res Inst, Birmingham B4 7ET, W Midlands, England
关键词
bio-oil; blending; supercritical; upgrading; characterisation; FAST PYROLYSIS; STORAGE STABILITY; BOILING-FRACTION; LIQUID FUEL; ESTERIFICATION; ETHANOL; BIOMASS; HYDRODEOXYGENATION; HYDROTREATMENT; HYDROGENATION;
D O I
10.1007/s11705-019-1861-9
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The work studied a non-catalytic upgrading of fast pyrolysis bio-oil by blending under supercritical conditions using methanol, ethanol and isopropanol as solvent and hydrogen donor. Characterisation of the bio-oil and the upgraded bio-oils was carried out including moisture content, elemental content, pH, heating value, gas chromatography-mass spectrometry (GCMS), Fourier transform infrared radiation, C-13 nuclear magnetic resonance spectroscopy, and thermogravimetric analysis to evaluate the effects of blending and supercritical reactions. The GCMS analysis indicated that the supercritical methanol reaction removed the acids in the bio-oil consequently the pH increased from 2.39 in the crude bio-oil to 4.04 after the supercritical methanol reaction. The ester contents increased by 87.49% after the supercritical methanol reaction indicating ester formation could be the major deacidification mechanism for reducing the acidity of the bio-oil and improving its pH value. Simply blending crude bio-oil with isopropanol was effective in increasing the C and H content, reducing the O content and increasing the heating value to 27.55 from 17.51 MJ center dot kg(-1) in the crude bio-oil. After the supercritical isopropanol reaction, the heating value of the liquid product slightly further increased to 28.85 MJ center dot kg(-1).
引用
收藏
页码:702 / 717
页数:16
相关论文
共 49 条
[1]   Effects of nano-structured CoMo catalysts on hydrodeoxygenation of fast pyrolysis oil in supercritical ethanol [J].
Ahmadi, Shima ;
Yuan, Zhongshun ;
Rohani, Sohrab ;
Xu, Chunbao .
CATALYSIS TODAY, 2016, 269 :182-194
[2]   Supercritical fluids in heterogeneous catalysis [J].
Baiker, A .
CHEMICAL REVIEWS, 1999, 99 (02) :453-473
[3]   Bio-oils obtained by vacuum pyrolysis of softwood bark as a liquid fuel for gas turbines. Part II: Stability and ageing of bio-oil and its blends with methanol and a pyrolytic aqueous phase [J].
Boucher, ME ;
Chaala, A ;
Pakdel, H ;
Roy, C .
BIOMASS & BIOENERGY, 2000, 19 (05) :351-361
[4]  
Boundy B., 2011, BIOMASS ENERGY DATA, P201
[5]   Review of fast pyrolysis of biomass and product upgrading [J].
Bridgwater, A. V. .
BIOMASS & BIOENERGY, 2012, 38 :68-94
[6]  
Bridgwater A.V., 2011, Thermochem. Process. Biomass Convers. into Fuels, Chem. Power, DOI DOI 10.1002/9781119990840.CH6
[7]   Characterization and separation of corn stover bio-oil by fractional distillation [J].
Capunitan, Jewel A. ;
Capareda, Sergio C. .
FUEL, 2013, 112 :60-73
[8]   Upgrading pyrolysis bio-oil through hydrodeoxygenation (HDO) using non-sulfided Fe-Co/SiO2 catalyst [J].
Cheng, Shouyun ;
Wei, Lin ;
Julson, James ;
Rabnawaz, Muhammad .
ENERGY CONVERSION AND MANAGEMENT, 2017, 150 :331-342
[9]   Competitive liquid biofuels from biomass [J].
Demirbas, Ayhan .
APPLIED ENERGY, 2011, 88 (01) :17-28
[10]   Additives to lower and stabilize the viscosity of pyrolysis oils during storage [J].
Diebold, JP ;
Czernik, S .
ENERGY & FUELS, 1997, 11 (05) :1081-1091