Optimization and characterization studies on bio-oil production from palm shell by pyrolysis using response surface methodology

被引:153
作者
Abnisa, Faisal [1 ]
Daud, W. M. A. Wan [1 ]
Sahu, J. N. [1 ]
机构
[1] Univ Malaya, Fac Engn, Dept Chem Engn, Kuala Lumpur 50603, Malaysia
关键词
Optimization; Bio-oil; Palm shell; Pyrolysis; Response surface methodology; AGRICULTURAL RESIDUES; BIOMASS; REACTOR; MALAYSIA; AMMONIA; ENERGY; WASTE; UREA; INDUSTRY; BAGASSE;
D O I
10.1016/j.biombioe.2011.05.011
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
In this work palm shell waste was pyrolyzed to produces bio-oil. The effects of several parameters on the pyrolysis efficiency were tested to identify the optimal bio-oil production conditions. The tested parameters include temperature, N(2) flow rate, feed-stock particle size, and reaction time. The experiments were conducted using a fix-bed reactor. The efficient response surface methodology (RSM), with a central composite design (CCD), were used for modeling and optimization the process parameters. The results showed that the second-order polynomial equation explains adequately the non-linear nature of the modeled response. An R(2) value of 0.9337 indicates a sufficient adjustment of the model with the experimental data. The optimal conditions found to be at the temperature of 500 degrees C, N(2) flow rate of 2 L/min, particle size of 2 mm and reaction time of 60 min and yield of bio-oil was approximately obtained 46.4 wt %. In addition, Fourier Transform infra-red (FT-IR) spectroscopy and gas chromatography/mass spectrometry (GC-MS) were used to characterize the gained bio-oil under the optimum condition. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:3604 / 3616
页数:13
相关论文
共 35 条
[1]   Utilization possibilities of palm shell as a source of biomass energy in Malaysia by producing bio-oil in pyrolysis process [J].
Abnisa, Faisal ;
Daud, W. M. A. Wan ;
Husin, W. N. W. ;
Sahu, J. N. .
BIOMASS & BIOENERGY, 2011, 35 (05) :1863-1872
[2]  
[Anonymous], 2000, DESIGN ANAL EXPT
[3]   Jute stick pyrolysis for bio-oil production in fluidized bed reactor [J].
Asadullah, M. ;
Rahman, M. Anisur ;
Ali, M. Mohsin ;
Motin, M. Abdul ;
Sultan, M. Borhanus ;
Alam, M. Robiul ;
Rahman, M. Sahedur .
BIORESOURCE TECHNOLOGY, 2008, 99 (01) :44-50
[4]   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
[5]   2K-P FRACTIONAL FACTORIAL DESIGNS .1. [J].
BOX, GE ;
HUNTER, JS .
TECHNOMETRICS, 1961, 3 (03) :311-&
[6]   ON THE EXPERIMENTAL ATTAINMENT OF OPTIMUM CONDITIONS [J].
BOX, GEP ;
WILSON, KB .
JOURNAL OF THE ROYAL STATISTICAL SOCIETY SERIES B-STATISTICAL METHODOLOGY, 1951, 13 (01) :1-45
[7]  
Bridgwater A.V., 2004, Thermal Science, V8, P21
[8]   Fast pyrolysis processes for biomass [J].
Bridgwater, AV ;
Peacocke, GVC .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2000, 4 (01) :1-73
[9]   Biomass for energy [J].
Bridgwater, Tony .
JOURNAL OF THE SCIENCE OF FOOD AND AGRICULTURE, 2006, 86 (12) :1755-1768
[10]   CALCULATION OF HIGHER HEATING VALUES OF BIOMASS MATERIALS AND WASTE COMPONENTS FROM ELEMENTAL ANALYSES [J].
BUCKLEY, TJ .
RESOURCES CONSERVATION AND RECYCLING, 1991, 5 (04) :329-341