Kinetic Study on Coal Char Combustion in a Microfluidized Bed

被引:30
作者
Fang, Yuan [1 ]
Zou, Renjie [1 ]
Luo, Guangqian [1 ]
Chen, Juan [1 ]
Li, Zehua [1 ]
Mao, Zhengjiang [1 ]
Zhu, Xianqing [1 ]
Peng, Fulei [1 ]
Guo, Shengqiang [1 ]
Li, Xian [1 ]
Yao, Hong [1 ]
机构
[1] Huazhong Univ Sci & Technol, SKLCC, Sch Energy & Power Engn, Wuhan 430074, Hubei, Peoples R China
基金
中国国家自然科学基金;
关键词
FLUIDIZED-BED; GASIFICATION EXPERIMENTS; SOLID REACTIONS; REACTIVITY; CO2; PARTICLES; BIOMASS; MODEL; TEMPERATURE; MECHANISM;
D O I
10.1021/acs.energyfuels.6b03137
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
The intrinsic kinetics of char combustion were commonly investigated using thermogravimetric analysis (TGA) in previous works at low temperatures to prevent oxygen limitations and temperature deviation. However, the low temperatures caused excess test time because the reaction rate was too slow. In this study, the microfluidized bed (MFB), which has effective heat and mass transfer, was used to investigate the intrinsic kinetics of char combustion at a higher temperature within less time. TGA was used to check the reliability of the MFB. The results suggested that, for fine particles (74-100 mu m), the particle temperature deviation and gas distortion could be disregarded in the MFB. For four coal samples, the activation energy measured by the MFB was similar to the result measured by TGA, but the test time using the MFB was greatly shortened as a result of the higher temperatures. The kinetic parameters measured by the MFB were used to predict the char oxidation rate. The predicted rate fit the TGA experiment well at lower temperatures. These results demonstrated the reliability of the MFB and TGA measurements. However, at higher temperatures, the combustion rate in TGA was limited by oxygen diffusion, suggesting that the TGA measurement should be carried out at relatively low temperatures to prevent oxygen diffusion limitation. Instead, the MFB measurement was still valid at higher temperatures as a result of the effective mass and heat transfer.
引用
收藏
页码:3243 / 3252
页数:10
相关论文
共 44 条
[1]  
Beeley T, 1996, TWENTY-SIXTH SYMPOSIUM (INTERNATIONAL) ON COMBUSTION, VOLS 1 AND 2, P3103
[2]  
BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
[3]   Combustion reactivity and morphological change in coal chars: Effect of pyrolysis temperature, heating rate and pressure [J].
Cai, HY ;
Guell, AJ ;
Chatzakis, IN ;
Lim, JY ;
Dugwell, DR ;
Kandiyoti, R .
FUEL, 1996, 75 (01) :15-24
[4]   Effect of pyrolysis conditions on the char gasification with mixtures of CO2 and H2O [J].
Chen, Chao ;
Wang, Jing ;
Liu, Wei ;
Zhang, Sen ;
Yin, Jingshu ;
Luo, Guangqian ;
Yao, Hong .
PROCEEDINGS OF THE COMBUSTION INSTITUTE, 2013, 34 :2453-2460
[5]   Kinetics of the gasification of a Rio Turbio coal under different pyrolysis temperatures [J].
De Micco, G. ;
Nasjleti, A. ;
Bohe, A. E. .
FUEL, 2012, 95 (01) :537-543
[6]   Reactivities of some biomass chars in air [J].
Di Blasi, C ;
Buonanno, F ;
Branca, C .
CARBON, 1999, 37 (08) :1227-1238
[7]   Combustion and gasification rates of lignocellulosic chars [J].
Di Blasi, Colomba .
PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2009, 35 (02) :121-140
[8]   Properties of high ash coal-char particles derived from inertinite-rich coal: II. Gasification kinetics with carbon dioxide [J].
Everson, Raymond C. ;
Neomagus, Hein W. J. P. ;
Kaitano, Rufaro ;
Falcon, Rosemary ;
du Cann, Vivien M. .
FUEL, 2008, 87 (15-16) :3403-3408
[9]   Kinetic analysis of non-isothermal thermogravimetric analyser results using a new method for the evaluation of the temperature integral and multi-heating rates [J].
Everson, RC ;
Neomagus, HWJP ;
Njapha, D .
FUEL, 2006, 85 (03) :418-422
[10]   The measurement of the rate of burning of different coal chars in an electrically heated fluidised bed of sand [J].
Fennell, P. S. ;
Kadchha, S. ;
Lee, H. -Y. ;
Dennis, J. S. ;
Hayhurst, A. N. .
CHEMICAL ENGINEERING SCIENCE, 2007, 62 (1-2) :608-618