Effects of various solvents on the liquefaction of biomass to produce fuels and chemical feedstocks

The liquefaction of pinewood in the presence of various solvents (water, acetone and ethanol) was studied so as to investigate the solvent effects on the biomass liquefaction process. Experiments were conducted in an autoclave in the conditions of temperature range 523-723 K, starting pressure 1 MPa, reaction time 20 min. biomass 10 g and solvent 60 g, respectively. The liquid products and solid residues were characterized by GC-MS and FTIR The results showed that the liquefaction products were greatly affected by the solvent type. With acetone as extraction agent, 4-methyl-1,2-benzenediol was one of the major compounds, while ethanol favored the formation of (E)-2-methoxy-4-(1-propenyl)-phenol and water significantly narrowed the products distribution. Among the tested solvents, acetone had the highest conversion rate, while the highest oil yield reached 26.5% at 473 K in ethanol. The FTIR analysis showed that cellulose liquefaction speed in water preceded in acetone and ethanol, and the solid residue consisted of solid carbon and a little amount of lignin fragments at 723 K. (c) 2008 Elsevier Ltd. All rights reserved.

[1]  D. Meier,et al.  State of the art of applied fast pyrolysis of lignocellulosic materials - a review , 1999 .

[2]  B. M. Kabyemela,et al.  Rapid and Selective Conversion of Glucose to Erythrose in Supercritical Water , 1997 .

[3]  T. Bhaskar,et al.  Effect of Rb and Cs carbonates for production of phenols from liquefaction of wood biomass , 2004 .

[4]  Thallada Bhaskar,et al.  Catalytic hydrothermal treatment of pine wood biomass: effect of RbOH and CsOH on product distribution , 2005 .

[5]  Ye Sun,et al.  Hydrolysis of lignocellulosic materials for ethanol production: a review. , 2002, Bioresource technology.

[6]  Esteban Chornet,et al.  Catalytic steam reforming of biomass-derived oxygenates: acetic acid and hydroxyacetaldehyde , 1996 .

[7]  T. Yamada,et al.  Rapid liquefaction of lignocellulosic waste by using ethylene carbonate , 1999 .

[8]  T. Bhaskar,et al.  Low-Temperature Hydrothermal Treatment of Biomass: Effect of Reaction Parameters on Products and Boiling Point Distributions , 2004 .

[9]  K. Ōuchi,et al.  Effect of pressure and temperature on the reaction of coal with alcohol-alkali , 1981 .

[10]  S. Yaman Pyrolysis of biomass to produce fuels and chemical feedstocks , 2004 .

[11]  B. C. Young,et al.  The rate of oxidation of char and coal in relation to their tendency to self-heat , 1979 .

[12]  Thallada Bhaskar,et al.  Low-temperature catalytic hydrothermal treatment of wood biomass: analysis of liquid products , 2005 .

[13]  Yong-jie Yan,et al.  Liquefaction of sawdust for liquid fuel , 1999 .

[14]  Atul K. Jain,et al.  Stability: Energy for a Greenhouse Planet Advanced Technology Paths to Global Climate , 2008 .

[15]  James E. Miller,et al.  Batch microreactor studies of lignin and lignin model compound depolymerization by bases in alcohol solvents , 1999 .

[16]  Ayhan Demirbas,et al.  Mechanisms of liquefaction and pyrolysis reactions of biomass , 2000 .

[17]  Michael Jerry Antal,et al.  Mechanism of formation of 2-furaldehyde from d-xylose , 1991 .

[18]  M. Küçük,et al.  Liquid products from Verbascum stalk by supercritical fluid extraction , 2001 .

[19]  A. Demirbas,et al.  Biomass resource facilities and biomass conversion processing for fuels and chemicals , 2001 .

[20]  V. Bisaria,et al.  Simultaneous bioconversion of cellulose and hemicellulose to ethanol. , 1998, Critical reviews in biotechnology.

[21]  H. Meuzelaar,et al.  Thermal Decomposition of Wood and Cellulose in the Presence of Solvent Vapors , 1997 .

[22]  S Pacala,et al.  Stabilization Wedges: Solving the Climate Problem for the Next 50 Years with Current Technologies , 2004, Science.