The effects of different catalysts on the pyrolysis of industrial wastes (olive and hazelnut bagasse)

被引:102
作者
Demiral, Ilknur [1 ]
Sensoz, Sevgi [1 ]
机构
[1] Eskisehir Osmangazi Univ, Fac Engn & Architecture, Dept Chem Engn, TR-26480 Eskisehir, Turkey
关键词
biomass; olive bagasse; hazelnut bagasse; catalytic pyrolysis; bio-oil;
D O I
10.1016/j.biortech.2008.03.053
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
Pyrolysis of olive and hazelnut bagasse biomass samples with two selected catalysts, namely activated alumina and sodium feldspar, have been conducted in a fixed-bed reactor. Experiments were carried out under certain pyrolysis conditions in a fixed-bed Heinze reactor. The catalyst was mixed with feedstock in different percentages. The effects of catalysts and their ratio (10%, 20%. 30% and 40% w/w) on the pyrolysis product yields were investigated and the results were compared with the results of experiments performed without catalyst under the same conditions. The maximum bio-oil yields for the bio-oils obtained from pyrolysis of olive bagasse were found as 37.07% and 36.67% on using activated alumina and sodium feldspar as catalysts, respectively, while these values were 27.64% and 31.68%, respectively, for the bio-oils from hazelnut bagasse. The oxygen contents of the bio-oils were also markedly reduced while the yield of bio-oil was reduced by the use of catalysts. The pyrolysis oils were examined using some spectroscopic and chromatographic analysis techniques. The results were compared with the petroleum fractions and the possibility of being a potential source of bio-oils was investigated. (C) 2008 Elsevier Ltd. All rights reserved.
引用
收藏
页码:8002 / 8007
页数:6
相关论文
共 37 条
[11]   Production and characterization of pyrolysis liquids from sunflower-pressed bagasse [J].
Gercel, HF .
BIORESOURCE TECHNOLOGY, 2002, 85 (02) :113-117
[12]   Bio-fuels from thermochemical conversion of renewable resources: A review [J].
Goyal, H. B. ;
Seal, Diptendu ;
Saxena, R. C. .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2008, 12 (02) :504-517
[13]  
HALL DO, 1982, BIOMASS ENERGY DEV C
[14]   PREMIUM QUALITY FUELS AND CHEMICALS FROM THE FLUIDIZED-BED PYROLYSIS OF BIOMASS WITH ZEOLITE CATALYST UPGRADING [J].
HORNE, PA ;
WILLIAMS, PT .
RENEWABLE ENERGY, 1994, 5 (5-8) :810-812
[15]   Upgrading of biomass-derived pyrolytic vapours over zeolite ZSM-5 catalyst: Effect of catalyst dilution on product yields [J].
Horne, PA ;
Williams, PT .
FUEL, 1996, 75 (09) :1043-1050
[16]   The fuel properties of pyrolysis liquid derived from urban solid wastes in Bangladesh [J].
Islam, MN ;
Islam, MN ;
Beg, MRA .
BIORESOURCE TECHNOLOGY, 2004, 92 (02) :181-186
[17]  
Jones MR, 1989, BIOMASS HDB, P97
[18]   Biomass pyrolysis in a circulating fluid bed reactor for the production of fuels and chemicals [J].
Lappas, AA ;
Samolada, MC ;
Iatridis, DK ;
Voutetakis, SS ;
Vasalos, IA .
FUEL, 2002, 81 (16) :2087-2095
[19]   Numerical modeling of combustion and pyrolysis of cellulosic biomass in thermogravimetric systems [J].
Liang, XH ;
Kozinski, JA .
FUEL, 2000, 79 (12) :1477-1486
[20]   Pyrolysis of wood/biomass for bio-oil: A critical review [J].
Mohan, Dinesh ;
Pittman, Charles U., Jr. ;
Steele, Philip H. .
ENERGY & FUELS, 2006, 20 (03) :848-889