Kinetics of coal char gasification with CO2: Impact of internal/external diffusion at high temperature and elevated pressure

被引:68
作者
Kim, Ryang-Gyoon [1 ]
Hwang, Chan-Won [1 ]
Jeon, Chung-Hwan [1 ]
机构
[1] Pusan Natl Univ, Dept Mech Engn, Pusan Clean Coal Ctr, Pusan, South Korea
关键词
Coal char; CO2; gasification; Kinetics; Reaction rate; Pressurized wire-heating reactor; COMBUSTION; MODEL; H2O; PARTICLES;
D O I
10.1016/j.apenergy.2014.05.011
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
A pressurized wire-heating reactor (PWHR) that can provide experimental conditions up to pressures and temperatures of 50 atm and 1750 K, respectively, was developed to evaluate the intrinsic reaction kinetics of CO2 gasification for Berau sub-bituminous coal char (Indonesian coal) at elevated pressure using a synchronized experimental method. This synchronization system consists of a thermocouple wire for both heating and direct measurement of the particle temperature and a photodetector sensor for measuring the intensity of the luminous emission from the reaction particle to determine the ignition/burnout points. The intrinsic reaction kinetics obtained from PWHR, which was analyzed from nth order reaction rate equations, was verified by comparison with TGA results. The internal/external effectiveness factor was analyzed to determine the effects of high pressure (up to 30 atm) and temperature (up to 1723 K) on char-CO2 gasification. Accordingly, the intrinsic activation energies based on nth order reaction rate equation were determined to be 152 kJ/mol (via TGA, 75 mu m char particle), 150 kJ/mol (via TGA, 800 mu m char particle), and 149.2 kJ/mol (via PWHR, 800 mu m char particle). (C) 2014 Elsevier Ltd. All rights reserved.
引用
收藏
页码:299 / 307
页数:9
相关论文
共 37 条
[1]   MODEL FOR DEVOLATILIZATION OF COAL PARTICLES IN FLUIDIZED-BEDS [J].
AGARWAL, PK ;
GENETTI, WE ;
LEE, YY .
FUEL, 1984, 63 (08) :1157-1165
[2]  
BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
[3]   Impact of finite-rate kinetics on carbon conversion in a high-pressure, single-stage entrained flow gasifier with coal-CO2 slurry feed [J].
Botero, Cristina ;
Field, Randall P. ;
Herzog, Howard J. ;
Ghoniem, Ahmed F. .
APPLIED ENERGY, 2013, 104 :408-417
[4]   Numerical investigation on performance of coal gasification under various injection patterns in an entrained flow gasifier [J].
Chen, Chih-Jung ;
Hung, Chen-I. ;
Chen, Wei-Hsin .
APPLIED ENERGY, 2012, 100 :218-228
[5]   REACTIVITY OF COAL AND CHAR .1. CARBON-DIOXIDE ATMOSPHERE [J].
DUTTA, S ;
WEN, CY ;
BELT, RJ .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (01) :20-30
[6]   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
[7]   Oxy-fuel combustion kinetics and morphology of coal chars obtained in N2 and CO2 atmospheres in an entrained flow reactor [J].
Gil, M. V. ;
Riaza, J. ;
Alvarez, L. ;
Pevida, C. ;
Pis, J. J. ;
Rubiera, F. .
APPLIED ENERGY, 2012, 91 (01) :67-74
[8]  
Higman C, 2008, GASIFICATION, 2ND EDITION, P1
[9]   CO2 gasification rate analysis of coal char in entrained flow coal gasifier [J].
Kajitani, S ;
Suzuki, N ;
Ashizawa, M ;
Hara, S .
FUEL, 2006, 85 (02) :163-169
[10]   Gasification rate analysis of coal char with a pressurized drop tube furnace [J].
Kajitani, S ;
Hara, S ;
Matsuda, H .
FUEL, 2002, 81 (05) :539-546