Effects of temperature on the formation of lignin-derived oligomers during the fast pyrolysis of Mallee woody biomass

被引:197
作者
Garcia-Perez, Manuel [1 ,2 ]
Wang, Shan [1 ]
Shen, Jun [1 ,3 ]
Rhodes, Martin [1 ]
Lee, Woo Jin [1 ]
Li, Chun-Zhu [1 ]
机构
[1] Monash Univ, Dept Chem Engn, Clayton, Vic 3800, Australia
[2] Washington State Univ, Dept Biol Syst Engn, Pullman, WA 99164 USA
[3] Taiyuan Univ Technol, Dept Chem Engn, Taiyuan 030024, Shanxi, Peoples R China
关键词
D O I
10.1021/ef7007634
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
This paper reports the evolution of the composition of bio-oil obtained from the fast pyrolysis of Mallee woody biomass as a function of temperature between 350 and 580 degrees C. Several analytical techniques were used to quantify bio-oil composition. For the volatile components, the results obtained by gas chromatography-mass spectrometry and Karl Fischer titration agree very well with those obtained by thermogravimetric analyses. However, for the heavy components, especially lignin-derived oligomers, synchronous UV-fluorescence spectroscopy and thermogravimetric analysis give more reliable results than the precipitation in cold water. Our results indicate that the accuracy of the precipitation methods to quantify lignin-derived oligomer in bio-oil is limited by the relatively large amounts of small oligomers remaining soluble in a metastable form in cold water. A maximum in the yield of lignin-derived oligomers was observed between 450 and 500 degrees C. In fact, most of the increases in the yield of bio-oil with increasing temperature above 350 degrees C can be explained by the formation of this type of oligomers. Increases in the rates at which the oligomers are formed and increases in their volatility at elevated temperature are the main reasons for the increased presence of oligomers in bio-oil produced at temperatures higher than 350 degrees C.
引用
收藏
页码:2022 / 2032
页数:11
相关论文
共 37 条
[1]   Inorganic compounds in biomass feedstocks .1. Effect on the quality of fast pyrolysis oils [J].
Agblevor, FA ;
Besler, S .
ENERGY & FUELS, 1996, 10 (02) :293-298
[2]   Characterization of the water-insoluble fraction from fast pyrolysis liquids (pyrolytic lignin) - Part III. Molar mass characteristics by SEC, MALDI-TOF-MS, LDI-TOF-MS, and Py-FIMS [J].
Bayerbach, Rolf ;
Nguyen, Van Dy ;
Schurr, Ulrich ;
Meier, Dietrich .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2006, 77 (02) :95-101
[3]   GC/MS characterization of liquids generated from low-temperature pyrolysis of wood [J].
Branca, C ;
Giudicianni, P ;
Di Blasi, C .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (14) :3190-3202
[4]   Multistep mechanism for the devolatilization of biomass fast pyrolysis oils [J].
Branca, Carmen ;
Di Blasi, Colomba .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (17) :5891-5899
[5]   An overview of fast pyrolysis of biomass [J].
Bridgwater, AV ;
Meier, D ;
Radlein, D .
ORGANIC GEOCHEMISTRY, 1999, 30 (12) :1479-1493
[6]   STABILITY OF WOOD FAST PYROLYSIS OIL [J].
CZERNIK, S ;
JOHNSON, DK ;
BLACK, S .
BIOMASS & BIOENERGY, 1994, 7 (1-6) :187-192
[7]  
Daugaard D. E., 2006, P SCI THERMAL CHEM B, P1189
[8]   Additives to lower and stabilize the viscosity of pyrolysis oils during storage [J].
Diebold, JP ;
Czernik, S .
ENERGY & FUELS, 1997, 11 (05) :1081-1091
[9]   Characterization of bio-oils in chemical families [J].
Garcia-Perez, M. ;
Chaala, A. ;
Pakdel, H. ;
Kretschmer, D. ;
Roy, C. .
BIOMASS & BIOENERGY, 2007, 31 (04) :222-242
[10]   Vacuum pyrolysis of softwood and hardwood biomass -: Comparison between product yields and bio-oil properties [J].
Garcia-Perez, M. ;
Chaala, A. ;
Pakdel, H. ;
Kretschmer, D. ;
Roy, C. .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2007, 78 (01) :104-116