Characteristics of cardboard and paper gasification with CO2

被引:71
作者
Ahmed, I. [1 ]
Gupta, A. K. [1 ]
机构
[1] Univ Maryland, Dept Mech Engn, Combust Lab, College Pk, MD 20742 USA
关键词
CO2; gasification; Cardboard gasification; Paper gasification; REACTION-KINETICS; CARBON-DIOXIDE; CHARS;
D O I
10.1016/j.apenergy.2009.04.002
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
Evolutionary behavior of syngas chemical composition and yield have been examined for paper and cardboard at three different temperatures of 800, 900 and 1000 degrees C using CO2 as the gasifying agent at constant flow rate. Specifically the evolution of syngas chemical composition with time has been investigated. Pyrolysis of the sample was dominant at the beginning of the gasification process as observed from the high initial devolatilization of the sample followed by char gasification of material to form syngas for a long period of time. Results provided the role of gasification temperature on kinetics of the CO2 gasification process. Increase in gasification temperature provided increased conversion of the sample material to syngas. Thus the sample conversion to syngas was low at the low temperature of 800 degrees C while at elevated temperatures of 900 and 1000 degrees C substantial enhancement of the kinetics process occurred. The evolution of extensive reaction rate of carbon-monoxide was calculated. Results show that increase in temperature increased the extensive reaction rate of carbon-monoxide. The global behavior of syngas chemical composition examined at three different temperatures revealed a peak in concentration of H-2 to exhibit after few minutes into the gasification that changed with gasification temperature. At 800 degrees C gasification temperature peak in H-2 was displayed at 3 min into gasification while it decreased to only 2 min, approximately, at gasification temperatures of 900 and 1000 degrees C. The effect of reactor temperature on CO mole fraction has also been examined. Increase in the gasification temperature enhances the mole fraction of CO yields. This is attributed to the increase in forward reaction rate of the Boudouard reaction (C + CO2 <-> 2CO). The results show important role of CO2 gas for the gasification of wastes and low grade fuels to clean syngas. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:2626 / 2634
页数:9
相关论文
共 14 条
[1]   Syngas yield during pyrolysis and steam gasification of paper [J].
Ahmed, I. ;
Gupta, A. K. .
APPLIED ENERGY, 2009, 86 (09) :1813-1821
[2]   Evolution of syngas from cardboard gasification [J].
Ahmed, I. ;
Gupta, A. K. .
APPLIED ENERGY, 2009, 86 (09) :1732-1740
[3]   Biomass gasification kinetics: Influences of pressure and char structure [J].
Cetin, E ;
Moghtaderi, B ;
Gupta, R ;
Wall, TF .
COMBUSTION SCIENCE AND TECHNOLOGY, 2005, 177 (04) :765-791
[4]   Pyrolysis/gasification of agricultural residues by carbon dioxide in the presence of different additives: influence of variables [J].
Encinar, JM ;
Beltran, FJ ;
Ramiro, A .
FUEL PROCESSING TECHNOLOGY, 1998, 55 (03) :219-233
[5]   Reaction kinetics of pulverized coal-chars derived from inertinite-rich coal discards: Gasification with carbon dioxide and steam [J].
Everson, RC ;
Neomagus, HWJP ;
Kasaini, H ;
Njapha, D .
FUEL, 2006, 85 (7-8) :1076-1082
[6]  
Higman C., 2003, GASIFICATION
[7]   Gasification potential and kinetics of Jordanian oil shales using CO2 as the reactant gas [J].
Jaber, JO ;
Probert, SD ;
Williams, PT ;
Tahat, M .
ENERGY SOURCES, 2000, 22 (06) :573-585
[8]   Effect of pyrolysis time on the gasification reactivity of char with CO2 at elevated temperatures [J].
Liu, H ;
Kaneko, M ;
Luo, CH ;
Kato, S ;
Kojima, T .
FUEL, 2004, 83 (7-8) :1055-1061
[9]  
Missen Ronald W., 1999, Introduction to Chemical Reaction Engineering and Kinetics
[10]  
MONTESINOS FM, 2002, FUEL, V81, P423