Mass transfer studies during CO2 gasification of torrefied and pyrolyzed chars

被引:31
作者
Vincent, Shubha Shalini [1 ]
Mahinpey, Nader [1 ]
Aqsha, Aqsha [1 ]
机构
[1] Univ Calgary, Schulich Sch Engn, Dept Chem & Petr Engn, Calgary, AB T2N 1N4, Canada
关键词
Gasification; Torrefied char; Pyrolyzed char; Kinetics; Diffusion; Mass transfer; BIOMASS GASIFICATION; PARTICLES; TORREFACTION; PRETREATMENT; COMBUSTION; KINETICS;
D O I
10.1016/j.energy.2013.12.034
中图分类号
O414.1 [热力学];
学科分类号
摘要
A comparative study on CO2 gasification kinetics of flax straw char produced by two different processes, namely, torrefaction and pyrolysis was investigated using a TGA (thermogravimetric analyzer). The objective of this research was to investigate the diffusion and surface reactions that occur during the CO2 gasification of the torrefied and pyrolyzed char particles. Gasification experiments were carried out at four different gasification temperatures from 750 to 900 degrees C and for different particle sizes (<90 mu m-925 mu m). The effects of temperature, particle size, and the char type on the rate of CO2 gasification were determined. The 50% conversion rate showed an increase in the reactivity values, along with an increase in the temperature, and decreased with an increase in the particle size for both the char types. The diffusional parameters such as effective diffusivity, effectiveness factor, and the DLI (diffusion limitation index) were calculated from the experimental data for both the char types. BET (Brunauer-Emmett-Teller) analysis and SEM (Scanning Electron Microscopy) analysis were performed to determine the surface area and to study the structural morphology of the char types. Torrefied char had a greater surface area than the pyrolyzed char. (C) 2013 Elsevier Ltd. All rights reserved.
引用
收藏
页码:319 / 327
页数:9
相关论文
共 23 条
[1]   Influence of torrefaction pretreatment on biomass gasification technology [J].
Chen Qing ;
Zhou JinSong ;
Liu BingJun ;
Mei QinFeng ;
Luo ZhongYang .
CHINESE SCIENCE BULLETIN, 2011, 56 (14) :1449-1456
[2]   Biomass resource facilities and biomass conversion processing for fuels and chemicals [J].
Demirbas, A .
ENERGY CONVERSION AND MANAGEMENT, 2001, 42 (11) :1357-1378
[3]   Combustion and gasification rates of lignocellulosic chars [J].
Di Blasi, Colomba .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2009, 35 (02) :121-140
[4]  
Dutta S, 1977, IND ENG CHEM PROC DD, P20
[5]   On the validity of thermogravimetric determination of carbon gasification kinetics [J].
Feng, B ;
Bhatia, SK .
CHEMICAL ENGINEERING SCIENCE, 2002, 57 (15) :2907-2920
[6]   Combustion and gasification characteristics of chars from raw and torrefied biomass [J].
Fisher, E. M. ;
Dupont, C. ;
Darvell, L. I. ;
Commandre, J. -M. ;
Saddawi, A. ;
Jones, J. M. ;
Grateau, M. ;
Nocquet, T. ;
Salvador, S. .
BIORESOURCE TECHNOLOGY, 2012, 119 :157-165
[7]   CO2 as a gasifying agent for gas production from pine sawdust at low temperatures using a Ni/Al coprecipitated catalyst [J].
Garcia, L ;
Salvador, ML ;
Arauzo, J ;
Bilbao, R .
FUEL PROCESSING TECHNOLOGY, 2001, 69 (02) :157-174
[8]  
Gobel B, 1999, P 4 BIOM C AM OAKL C, P1025
[9]   Diffusional effects in CO2 gasification experiments with single biomass char particles.: 1.: Experimental investigation [J].
Gomez-Barea, A. ;
Ollero, P. ;
Fernandez-Baco, C. .
ENERGY & FUELS, 2006, 20 (05) :2202-2210
[10]   Diffusional effects in CO2 gasification experiments with single biomass char particles.: 2.: Theoretical predictions [J].
Gomez-Barea, A. ;
Ollero, P. ;
Villanueva, A. .
ENERGY & FUELS, 2006, 20 (05) :2211-2222