Hydrodeoxygenation of Lignocellulosic Fast Pyrolysis Bio-Oil: Characterization of the Products and Effect of the Catalyst Loading Ratio

被引:35
作者
Benes, Mario [1 ]
Bilbao, Rafael [1 ]
Machado Santos, Jandyson [3 ,4 ]
Melo, Josue Alves [3 ]
Wisniewski, Alberto, Jr. [4 ]
Fonts, Isabel [1 ,2 ]
机构
[1] Univ Zaragoza, Aragon Inst Engn Res I3A, Chem & Environm Engn Dept, Thermochem Proc Grp, Zaragoza 50018, Spain
[2] Ctr Univ Def, Chem & Environm Dept, Zaragoza 50091, Spain
[3] Univ Fed Rural Pernambuco, Chem Dept, BR-52171900 Recife, PE, Brazil
[4] Univ Fed Sergipe, Chem Dept, Petr & Energy Biomass Res Grp PEB, BR-49100000 Sao Cristovao, Sergipe, Brazil
关键词
TRANSPORTATION FUELS; ADVANCED BIOFUELS; FUNCTIONAL-GROUPS; HYDROTREATMENT; BIOMASS; FEEDSTOCKS; FRACTIONS; WATER; QUANTIFICATION; TEMPERATURE;
D O I
10.1021/acs.energyfuels.9b00265
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 hydrodeoxygenation (HDO) of bio-oil at 350 degrees C and 200 bar in a batch reactor over a Ru/C catalyst has been studied experimentally with the aim of contributing to the understanding of the HDO reaction and its effect on the physicochemical properties of the organic liquid fraction obtained. Moreover, the effect of the catalyst loading ratio used in the HDO treatment and a previous stabilization stage carried out at 250 degrees C have also been assessed. Under the studied operational conditions, reactions of decarboxylation, HDO, polymerization, decarbonylation, methanation, demethylation, and pyrolytic lignin depolymerization took place during the HDO process. In these experiments, O was removed from the bio-oil mainly in the form of CO2 (15-26 g of CO2.100 g(-1) of dry bio-oil) and also as H2O (1.8-5.8 g of H2O.100 g(-1) of dry bio-oil). The consumption of H-2 was between 0.75 and 1.0 g.100 g(-1) of dry bio-oil. A comparison of the physicochemical properties of the raw bio-oil and the HDO organic phases shows that the major effects of HDO are a reduction in the O content from 34 to 13 wt %, an increase in the higher heating value (dry basis) from 24.3 to 35.5 MJ.kg(-1), lower polarity of the organic compounds determined by the significant increase in the hexane solubility, lower corrosiveness evidenced by the smaller total acid number and acid concentrations, and a marked change in the gas chromatography-mass spectrometry detectable compounds, increasing the presence of monophenols and cyclic ketones and decreasing the presence of levoglucosan, methoxyphenols, and furans. Electrospray ionization(+/-)-FTMS analyses of the raw bio-oil and the HDO liquid fractions show a widespread reduction of the O/C molar ratio of the compounds, an efficient deoxygenation and depolymerization of pyrolytic lignin, and a nondesirable increase in the range of molecular weights of the organic molecules after the HDO treatment.
引用
收藏
页码:4272 / 4286
页数:15
相关论文
共 49 条
  • [1] Techno-economic comparison of biomass-to-transportation fuels via pyrolysis, gasification, and biochemical pathways
    Anex, Robert P.
    Aden, Andy
    Kazi, Feroz Kabir
    Fortman, Joshua
    Swanson, Ryan M.
    Wright, Mark M.
    Satrio, Justinus A.
    Brown, Robert C.
    Daugaard, Daren E.
    Platon, Alex
    Kothandaraman, Geetha
    Hsu, David D.
    Dutta, Abhijit
    [J]. FUEL, 2010, 89 : S29 - S35
  • [2] Catalytic hydrotreatment of fast-pyrolysis oil using non-sulfided bimetallic Ni-Cu catalysts on a δ-Al2O3 support
    Ardiyanti, A. R.
    Khromova, S. A.
    Venderbosch, R. H.
    Yakovlev, V. A.
    Heeres, H. J.
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2012, 117 : 105 - 117
  • [3] Hydrotreatment of wood-based pyrolysis oil using zirconia-supported mono- and bimetallic (Pt, Pd, Rh) catalysts
    Ardiyanti, A. R.
    Gutierrez, A.
    Honkela, M. L.
    Krause, A. O. I.
    Heeres, H. J.
    [J]. APPLIED CATALYSIS A-GENERAL, 2011, 407 (1-2) : 56 - 66
  • [4] Characterization of the water-insoluble fraction from fast pyrolysis liquids (pyrolytic lignin). Part IV: Structure elucidation of oligomeric molecules
    Bayerbach, Rolf
    Meier, Dietrich
    [J]. JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2009, 85 (1-2) : 98 - 107
  • [5] Compositional Changes during Hydrodeoxygenation of Biomass Pyrolysis Oil
    Bi, Yantao
    Wang, Gang
    Shi, Quan
    Xu, Chunming
    Gao, Jinsen
    [J]. ENERGY & FUELS, 2014, 28 (04) : 2571 - 2580
  • [6] Influence of feedstock, catalyst, pyrolysis and hydrotreatment temperature on the composition of upgraded oils from intermediate pyrolysis
    Boscagli, Chiara
    Morgano, Marco Tomasi
    Raffelt, Klaus
    Leibold, Hans
    Grunwaldt, Jan-Dierk
    [J]. BIOMASS & BIOENERGY, 2018, 116 : 236 - 248
  • [7] Reactivity of platform molecules in pyrolysis oil and in water during hydrotreatment over nickel and ruthenium catalysts
    Boscagli, Chiara
    Raffelt, Klaus
    Grunwaldt, Jan-Dierk
    [J]. BIOMASS & BIOENERGY, 2017, 106 : 63 - 73
  • [8] Aromatic Production from Catalytic Fast Pyrolysis of Biomass-Derived Feedstocks
    Carlson, Torren R.
    Tompsett, Geoffrey A.
    Conner, William C.
    Huber, George W.
    [J]. TOPICS IN CATALYSIS, 2009, 52 (03) : 241 - 252
  • [9] Analysis of Oxygenated Compounds in Hydrotreated Biomass Fast Pyrolysis Oil Distillate Fractions
    Christensen, Earl D.
    Chupka, Gina M.
    Luecke, Jon
    Smurthwaite, Tricia
    Alleman, Teresa L.
    Iisa, Kristiina
    Franz, James A.
    Elliott, Douglas C.
    McCormick, Robert L.
    [J]. ENERGY & FUELS, 2011, 25 (11) : 5462 - 5471
  • [10] Stability of an acid activated carbon based bifunctional catalyst for the raw bio-oil hydrodeoxygenation
    Cordero-Lanzac, Tomas
    Palos, Roberto
    Arandes, Jose M.
    Castano, Pedro
    Rodriguez-Mirasol, Jose
    Cordero, Tomas
    Bilbao, Javier
    [J]. APPLIED CATALYSIS B-ENVIRONMENTAL, 2017, 203 : 389 - 399