Influence of temperature and alumina catalyst on pyrolysis of corncob

被引:103
作者
Ates, Funda [1 ]
Isikdag, M. Asli [2 ]
机构
[1] Anadolu Univ, Dept Chem Engn, Fac Engn & Architecture, TR-26555 Eskisehir, Turkey
[2] Bilecik Univ, Bilecik, Turkey
关键词
Corncob; Catalyst; Pyrolysis; Fuel; Chemical raw materials; BIOMASS FAST PYROLYSIS; FIXED-BED REACTOR; BIO-OIL; TRANSPORTATION FUELS; HYDROCARBONS; CHEMICALS; SAMPLES; BEHAVIOR; WASTES; ENERGY;
D O I
10.1016/j.fuel.2009.03.008
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
Corncob has been investigated as an alternative feedstock to obtain fuels and chemicals via pyrolysis in fixed-bed reactor. The influence of pyrolysis temperature in the range 300-800 degrees C as well as the catalyst effects on the products was investigated in detail and the obtained results were compared. The results indicated that a maximum oil yield of 22.2% was obtained at a moderate temperature of 600 degrees C. The oil yield was reduced when the temperature was increased from 600 to 800 degrees C, whereas the gas yield increased. Pyrolysis oils were examined by using instrumental analysis, H-1 NMR spectroscopy and GC/MS. This analysis revealed that the pyrolysis oils were chemically very heterogeneous at all temperatures. It was determined that the most abundant compounds composing the bio-oil were phenolics. It was observed that the catalyst decreased the reaction temperature. Most of the components obtained using a catalyst at moderate temperatures was close to those obtained at high temperatures without using a catalyst. Moreover, the use of a catalyst and the high temperatures of the reactions also decreased the amount of oxygenated compounds produced. According to these results, corncob bio-oils can be used as fuel and constitute a valuable source of chemical raw materials. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1991 / 1997
页数:7
相关论文
共 35 条
[1]   PRODUCTION OF HYDROCARBONS BY CATALYTIC UPGRADING OF A FAST PYROLYSIS BIO-OIL .1. CONVERSION OVER VARIOUS CATALYSTS [J].
ADJAYE, JD ;
BAKHSHI, NN .
FUEL PROCESSING TECHNOLOGY, 1995, 45 (03) :161-183
[2]   PRODUCTION OF HYDROCARBONS BY CATALYTIC UPGRADING OF A FAST PYROLYSIS BIO-OIL .2. COMPARATIVE CATALYST PERFORMANCE AND REACTION PATHWAYS [J].
ADJAYE, JD ;
BAKHSHI, NN .
FUEL PROCESSING TECHNOLOGY, 1995, 45 (03) :185-202
[3]  
AGARWAL AK, 1999, TERI INFORM MONITOR, V4, P1
[4]   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
[5]   Evaluation of various types of Al-MCM-41 materials as catalysts in biomass pyrolysis for the production of bio-fuels and chemicals [J].
Antonakou, Eleni ;
Lappas, Angelos ;
Nilsen, Merete H. ;
Bouzga, Aud ;
Stocker, Michael .
FUEL, 2006, 85 (14-15) :2202-2212
[6]   Evaluation of the role of the pyrolysis temperature in straw biomass samples and characterization of the oils by GUMS [J].
Ates, Funda ;
Isikdag, Muejde Asli .
ENERGY & FUELS, 2008, 22 (03) :1936-1943
[7]   Pyrolysis of two different biomass samples in a fixed-bed reactor combined with two different catalysts [J].
Ates, Funda ;
Putun, Ayse E. ;
Putun, Ersan .
FUEL, 2006, 85 (12-13) :1851-1859
[8]   Influence of temperature and heating rate on the fixed bed pyrolysis of meat and bone meal [J].
Ayllon, M. ;
Aznar, M. ;
Sanchez, J. L. ;
Gea, G. ;
Arauzo, J. .
CHEMICAL ENGINEERING JOURNAL, 2006, 121 (2-3) :85-96
[9]  
BASCETINCELIK A, 2005, P 9 INT C MECH EN AG
[10]   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