Mechanism of palm oil waste pyrolysis in a packed bed

被引:144
作者
Yang, Haiping
Yan, Rong
Chen, Hanping
Lee, Dong Ho
Liang, David Tee
Zheng, Chuguang
机构
[1] Huazhong Univ Sci & Technol, State Key Lab Coal Combust, Wuhan 430074, Peoples R China
[2] Nanyang Technol Univ, Inst Environm Sci & Engn, Innovat Ctr, Singapore 637723, Singapore
关键词
D O I
10.1021/ef0600311
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
To better understand the process mechanism, pyrolysis of palm oil wastes was investigated at different temperatures in a packed bed, with focus on the changing of chemical structure and physical characteristics of solid residues and gas-releasing properties. First, three palm oil wastes were pyrolyzed with temperature increasing from the ambient to 1000 degrees C, and the main products from it were solid charcoal, liquid oil, and hydrogen-rich gas. The gas component mainly consisted of H-2, CO2, CO, and CH4 together with trace C2H4 and C2H6. CO and CO2 evolved out at lower temperature (< 450 degrees C), while H-2 released at higher temperature ( 600- 700 degrees C). Second, the decomposition property of biomass shell was analyzed at variable temperatures ( 300, 400,..., 1000 degrees C). The pyrolysis products were thoroughly identified using various approaches ( including micro-GC, FTIR, GC-MS, ASAP2010, SEM, and CNHS/O analyzer) to understand the influence of temperature on product properties and, thus, reaction mechanism involved. Starting from low temperature at 300 degrees C, CO and CO2 evolved out easily because of the breaking of carbonyl and carboxyl functional groups, and the releasing of CH4 increased at the price of CH alkyl breaking and diminishing. Following that, at temperature > 400 degrees C, aromatic rings broke gradually with a lot of H-2 evolving out. Meanwhile, a large amount of pores in the biomass sample were opened in the course of pyrolysis, and the Brunauer-Emmett-Teller ( BET) surface area increased greatly. The maximum yield of oil was achieved at 500 degrees C, and it is a mixture of acid, ether, phenol, etc. High temperature (> 700 degrees C) was favorable for the evolving of hydrogen-rich gases, while medium temperature (500-600 degrees C) was recommendable for a higher generation of liquid oil and charcoal with a large BET surface area and fine pore size.
引用
收藏
页码:1321 / 1328
页数:8
相关论文
共 20 条
[1]   Fixed bed pyrolysis of Euphorbia rigida with different catalysts [J].
Ates, F ;
Pütün, AE ;
Pütün, E .
ENERGY CONVERSION AND MANAGEMENT, 2005, 46 (03) :421-432
[2]   Fourier transform infrared spectroscopic study of thermal degradation of sugar cane bagasse [J].
Bilba, K ;
Ouensanga, A .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1996, 38 :61-73
[3]   Biomass pyrolysis/gasification for product gas production: the overall investigation of parametric effects [J].
Chen, G ;
Andries, J ;
Luo, Z ;
Spliethoff, H .
ENERGY CONVERSION AND MANAGEMENT, 2003, 44 (11) :1875-1884
[4]   Bio oil from pyrolysis of cashew nut shell-characterisation and related properties [J].
Das, P ;
Sreelatha, T ;
Ganesh, A .
BIOMASS & BIOENERGY, 2004, 27 (03) :265-275
[5]   An overview of Biomass pyrolysis [J].
Demirbas, A ;
Arin, G .
ENERGY SOURCES, 2002, 24 (05) :471-482
[6]   Biomass resource facilities and biomass conversion processing for fuels and chemicals [J].
Demirbas, A .
ENERGY CONVERSION AND MANAGEMENT, 2001, 42 (11) :1357-1378
[7]   A review of the primary measures for tar elimination in biomass gasification processes [J].
Devi, L ;
Ptasinski, KJ ;
Janssen, FJJG .
BIOMASS & BIOENERGY, 2003, 24 (02) :125-140
[8]   Product distribution from pyrolysis of wood and agricultural residues [J].
Di Blasi, C ;
Signorelli, G ;
Di Russo, C ;
Rea, G .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1999, 38 (06) :2216-2224
[9]   Pyrolysis behavior and kinetics of biomass derived materials [J].
Fisher, T ;
Hajaligol, M ;
Waymack, B ;
Kellogg, D .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2002, 62 (02) :331-349
[10]   GAS-PRODUCTION BY PYROLYSIS OF MUNICIPAL SOLID-WASTE AT HIGH-TEMPERATURE IN A FLUIDIZED-BED REACTOR [J].
GARCIA, AN ;
FONT, R ;
MARCILLA, A .
ENERGY & FUELS, 1995, 9 (04) :648-658