GC/MS characterization of liquids generated from low-temperature pyrolysis of wood

被引:359
作者
Branca, C [1 ]
Giudicianni, P [1 ]
Di Blasi, C [1 ]
机构
[1] Univ Naples Federico II, Dipartimento Ingn Chim, I-80125 Naples, Italy
关键词
FLASH PYROLYSIS; MOLECULAR CHARACTERIZATION; PRODUCT DISTRIBUTION; BED REACTOR; BIOMASS; KINETICS; LIGNIN; OIL; PARTICLE; YIELDS;
D O I
10.1021/ie030066d
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
Conventional pyrolysis of beech wood has been carried out for heating temperatures in the range 600-900 K, reproducing conditions of interest in countercurrent fixed-bed gasification. The yields of liquids (water and tars) increase with the heating temperature from about 40 to 55% of dry wood mass, confirming results previously obtained with a laboratory-scale gasifier. Apart from qualitative identification of similar to90 species, GC/MS techniques have been applied to quantify 40-43% of tars (40 species, with major contributions from acetic acid, hydroxypropanone, hydroxyacetaldehyde, levoglucosan, formic acid, syringol, and 2-furaldehyde). Decomposition of holocellulose leads to the formation of furan derivatives and carbohydrates, with a temperature-dominated selectivity toward hydroxyacetaldehyde against levoglucosan. Syringols and guaiacols, originating from primary degradation of lignin, present a maximum for heating temperatures of about 750-800 K whereas, owing to secondary degradation, phenols continuously increase. A comparison is also provided with fast pyrolysis liquids obtained from four commercial plants.
引用
收藏
页码:3190 / 3202
页数:13
相关论文
共 61 条
[1]
Pyrolysis of sawdust in a conical spouted bed reactor.: Yields and product composition [J].
Aguado, R ;
Olazar, M ;
José, MJS ;
Aguirre, G ;
Bilbao, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2000, 39 (06) :1925-1933
[2]
CELLULOSE PYROLYSIS KINETICS - THE CURRENT STATE KNOWLEDGE [J].
ANTAL, MJ ;
VARHEGYI, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1995, 34 (03) :703-717
[3]
AVNI E, 1985, FUNDAMENTALS THERMOC, P329, DOI DOI 10.1007/978-94-009-4932-4
[4]
INFLUENCE OF PHYSICAL AND CHEMICAL-PARAMETERS ON WOOD PYROLYSIS [J].
BEAUMONT, O ;
SCHWOB, Y .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1984, 23 (04) :637-641
[5]
BEENACKERS AAC, 1996, 9 EUR BIOEN C, P228
[6]
Analysis of the combustion kinetics and thermal behavior of an intumescent system [J].
Branca, C ;
Di Blasi, C ;
Horacek, H .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (09) :2107-2114
[7]
BRIDGWATER AV, 2001, PROGR THERMOCHEMICAL, V1, P977
[8]
Buekens AG, 1990, 12736 EUR COMM EUR C
[9]
Bühler R, 1997, BIOMASS GASIFICATION AND PYROLYSIS: STATE OF THE ART AND FUTURE PROSPECTS, P117
[10]
Study of the primary pyrolysis of Kraft lignin at high heating rates: Yields and kinetics [J].
Caballero, JA ;
Font, R ;
Marcilla, A .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1996, 36 (02) :159-178