Fast Pyrolysis of African and European Lignocellulosic Biomasses Using Py-GC/MS and Fluidized Bed Reactor

被引:149
作者
Azeez, Akeem M. [2 ,3 ]
Meier, Dietrich [1 ]
Odermatt, Juergen [3 ]
Willner, Thomas [4 ]
机构
[1] vTI, Inst Wood Technol & Wood Biol, D-21031 Hamburg, Germany
[2] Univ Ado Ekiti, Dept Chem, Ado Ekiti, Nigeria
[3] Univ Hamburg, D-21031 Hamburg, Germany
[4] Hamburg Univ Appl Sci, Fac Life Sci, D-21031 Hamburg, Germany
关键词
WATER-INSOLUBLE FRACTION; MALLEE WOODY BIOMASS; CONVERSION PROCESSES; BIO-OIL; OBTAINING 1,6-ANHYDROSACCHARIDES; TEMPERATURE; LIGNIN; PRETREATMENT; MECHANISMS; PRODUCTS;
D O I
10.1021/ef9012856
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
Five biomasses spruce (Picea abies L.), beech (Fagus sylvatica L.), iroko (Chlophora excelsa L.), albizia (Albizia adianthifolia L.), and corncob (Zen mays ssp.) have been subjected to analytical pyrolysis (Py-GC/MS) and bench-scale pyrolysis with a fluidized bed reactor at 470 degrees C. The comparison of Py-GC/MS and bench scale results revealed only small differences in the relative concentration of single products mainly acetic acid, hydroxyacetaldehyde, hydroxypropanone, and lignin-derived guaiacyl and syringyl components. For European woods, organic oil yields were approximately 57%, whereas African biomasses yielded between 41 and 48% because of their higher mineral contents. The analysis of bio-oil composition revealed no significant differences between African and European biomasses. Acetic acid, hydroxyacetaldehyde, hydroxypropanone, and levoglucosan were found to be the largest individual components in the volatiles. Bio-oil from corncob, having the lowest lignin content contained high concentration of 4-vinylphenol, a lignin derived product. This implied that the degradation products largely depend on the constituents' structure of the biomass. The higher heating value of all bio-oils ranged 16-17 MJ/kg.
引用
收藏
页码:2078 / 2085
页数:8
相关论文
共 42 条
[1]   Pyrolysis of softwood carbohydrates in a fluidized bed reactor [J].
Aho, Atte ;
Kumar, Narendra ;
Eranen, Kari ;
Holmbom, Bjarne ;
Hupa, Mikko ;
Salmi, Tapio ;
Murzin, Dmitry Yu. .
INTERNATIONAL JOURNAL OF MOLECULAR SCIENCES, 2008, 9 (09) :1665-1675
[2]  
AINA OM, 2006, INT C REN EN DEV COU
[3]  
Andreae M.O., 1991, GLOBAL BIOMASS BURNI, P2
[4]  
[Anonymous], 1984, WOOD CHEM ULTRASTRUC, DOI DOI 10.1515/9783110839654
[5]   Mechanisms of thermochemical biomass conversion processes. Part 1: Reactions of pyrolysis [J].
Balat, M. .
ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2008, 30 (07) :620-635
[6]   Mechanisms of thermochemical biomass conversion processes. Part 3: Reactions of liquefaction [J].
Balat, M. .
ENERGY SOURCES PART A-RECOVERY UTILIZATION AND ENVIRONMENTAL EFFECTS, 2008, 30 (07) :649-659
[7]   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
[8]   Characterization of the water-insoluble fraction from fast pyrolysis liquids (pyrolytic lignin). Part IV: Structure elucidation of oligomeric molecules [J].
Bayerbach, Rolf ;
Meier, Dietrich .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2009, 85 (1-2) :98-107
[9]   Fast pyrolysis processes for biomass [J].
Bridgwater, AV ;
Peacocke, GVC .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2000, 4 (01) :1-73
[10]   Principles and practice of biomass fast pyrolysis processes for liquids [J].
Bridgwater, AV .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1999, 51 (1-2) :3-22