Coke solution-loss degradation model with non-equimolar diffusion and changing local pore structure

被引:23
作者
Huang, Junchen [1 ,2 ]
Guo, Rui [3 ]
Wang, Qi [1 ,2 ]
Liu, Zhongsuo [1 ,2 ]
Zhang, Song [1 ,2 ]
Sun, Jiafu [1 ,2 ]
机构
[1] Univ Sci & Technol Liaoning, Sch Met & Mat, Anshan 114051, Liaoning, Peoples R China
[2] Univ Sci & Technol Liaoning, Key Lab Chem Met Engn Liaoning Prov, Anshan 114051, Liaoning, Peoples R China
[3] North China Univ Sci & Technol, Coll Chem Engn, Tangshan 063210, Hebei, Peoples R China
基金
中国国家自然科学基金;
关键词
Model; Coke-quality evaluation; Solution-loss behavior; Degradation behavior; Non-equimolar diffusion; Local pore structure; FLUID-SOLID REACTIONS; METALLURGICAL COKE; CHAR PARTICLE; STEFAN FLOW; COAL CHAR; GASIFICATION; COMBUSTION; BEHAVIOR; KINETICS;
D O I
10.1016/j.fuel.2019.116694
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
To provide a more accurate reference for coke quality evaluation, and to achieve the benefits of coking-coal resource use and energy conservation, a coke solution-loss degradation model was developed by combining non-equimolar diffusion, the parallel pore model, the random pore model and an ever-changing local pore structure. The model could predict the coke solution-loss behavior and degradation behavior to improve the understanding of the coke solution-loss degradation mechanism. The model is of value for application by coking and ironmaking workers. The model was verified by the coke overall weight-loss(%) and local porosity after reaction. The predicted results showed a good fit with the experimental data. The CO2 concentration on the coke outer surface and the CO2 concentration distribution in the inner coke decreased because of the effect of non-equimolar diffusion. The coke solution-loss behavior and degradation behavior were presented by a three-dimensional diagram of CO2 concentration and the local inner coke porosity, respectively. The model was verified by the effectiveness factor and coke strength after reaction (CSR25) separately, and the conclusion could be drawn that the gradient distribution of the CO2 concentration and local-porosity inner coke could cause the greatest degradation and yield the worst coke strength after reaction.
引用
收藏
页数:12
相关论文
共 51 条
[1]  
Aderibigbe D.A., 1981, Ironmaking and steelmaking, V1, P11
[2]  
[Anonymous], 1996, 3 EUR IR C P
[3]  
BHATIA SK, 1980, AICHE J, V26, P379, DOI 10.1002/aic.690260308
[4]   A RANDOM PORE MODEL FOR FLUID-SOLID REACTIONS .2. DIFFUSION AND TRANSPORT EFFECTS [J].
BHATIA, SK ;
PERLMUTTER, DD .
AICHE JOURNAL, 1981, 27 (02) :247-254
[5]  
Bird R B., 2002, Transportphenomena
[6]   Phase and mineral behavior of coke in cohesive zone [J].
Chang, Zhiyu ;
Zhang, Jianliang ;
Ning, Xiaojun .
FUEL, 2019, 253 :32-39
[7]  
CHAPMAN S., 1952, The Mathematical Theory of Non-Uniform Gases
[8]  
Diez MA, 2016, ENCY IRON STEEL THEI, P2234
[9]   THE IMPORTANCE OF PORE STRUCTURE AND DIFFUSION IN THE KINETICS OF GAS-SOLID NON-CATALYTIC REACTIONS - REACTION OF CALCINED LIMESTONE WITH SO2 [J].
DOGU, T .
CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1981, 21 (03) :213-222
[10]   Combustion modelling opportunities and challenges for oxy-coal carbon capture technology [J].
Edge, P. ;
Gharebaghi, M. ;
Irons, R. ;
Porter, R. ;
Porter, R. T. J. ;
Pourkashanian, M. ;
Smith, D. ;
Stephenson, P. ;
Williams, A. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2011, 89 (09) :1470-1493