Effect of pyrolysis time on the gasification reactivity of char with CO2 at elevated temperatures

被引:53
作者
Liu, H
Kaneko, M
Luo, CH
Kato, S
Kojima, T
机构
[1] Seikei Univ, Dept Appl Chem, Musashino, Tokyo 1808633, Japan
[2] New Energy & Ind Dev Org, Toshima Ku, Tokyo, Japan
关键词
coal char; gasification; pyrolysis; fluidized bed reactor; elevated temperature;
D O I
10.1016/S0016-2361(03)00142-X
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
Gasification of a char has so far been mainly studied at low temperatures and low heating rates with a TGA (thermogravimetric analyzer). Studies on gasification of a char in CO2 at elevated temperatures and high heating rates are necessary to develop IGCC technology. With a unique fluidized bed. the effect of pyrolysis time on char reactivity was investigated. It was found that a longer pyrolysis time led to lower reactivity of a char, while this effect leveled off as pyrolysis time increased. The pyrolysis time also had an influence on the temperature dependence of gasification reactivity. Initial char gasification rate decreased as pyrolysis time increased. The pyrolysis time had effect on the entire process of char gasification. The effect of pyrolysis time was more remarkable for a coal with high volatile matter content among the three coals tested. The gasification rate of a char was very different from that of a raw coal (gasification without pyrolysis in advance), which suggested an influence of pyrolysis time and atmosphere on char reactivity. Accordingly, those results obtained from a TGA are necessary to be corrected when applied to a practical entrained flow gasifier. (C) 2004 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1055 / 1061
页数:7
相关论文
共 17 条
[1]   Thermogravimetric determination of the carbon dioxide reactivity of char from some New Zealand coals and its association with the inorganic geochemistry of the parent coal [J].
Beamish, BB ;
Shaw, KJ ;
Rodgers, KA ;
Newman, J .
FUEL PROCESSING TECHNOLOGY, 1998, 53 (03) :243-253
[2]   On the scaling-up of a two-stage air blown entrained flow coal gasifier [J].
Chen, CX ;
Miyoshi, T ;
Kamiya, H ;
Horio, M ;
Kojima, T .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (04) :745-750
[3]   Gasification of biomass chars in air - Effect of heat treatment temperature [J].
Devi, TG ;
Kannan, MP .
ENERGY & FUELS, 2000, 14 (01) :127-130
[4]  
JAHNKE FC, 1907, P ADV CLEAN COAL TEC, P111
[5]  
JAN WN, 1998, FUEL PROCESS TECHNOL, V56, P89
[6]  
KAJITANI S, 1998, W97020 CENTR RES I E
[7]   EFFECTS OF COAL CARBONIZATION CONDITIONS ON RATE OF STEAM GASIFICATION OF CHAR [J].
KASAOKA, S ;
SAKATA, Y ;
SHIMADA, M .
FUEL, 1987, 66 (05) :697-701
[8]   MEASUREMENT OF GASIFICATION RATE OF COAL CHAR USING A FLUIDIZED-BED [J].
KOJIMA, T ;
FURUSAWA, T ;
KUNII, D .
KAGAKU KOGAKU RONBUNSHU, 1984, 10 (05) :596-601
[9]   EXPERIMENTAL AND THEORETICAL INVESTIGATION OF EXPERIMENTAL FLUIDIZED-BED CHAR GASIFIER BY MODEL TAKING ACCOUNT OF ADSORPTION DYNAMICS OF REACTANT [J].
KOJIMA, T ;
ADSCHIRI, T ;
KAWAGUCHI, H ;
FURUSAWA, T .
CHEMICAL ENGINEERING SCIENCE, 1986, 41 (04) :813-820
[10]   EFFECTS OF DEVOLATILIZATION CONDITION ON GASIFICATION RATE OF COAL CHAR [J].
KOJIMA, T ;
YAMASHITA, S ;
FURUSAWA, T .
KAGAKU KOGAKU RONBUNSHU, 1985, 11 (06) :735-738