Drying kinetics characteristics of lignite using thermogravimetric analysis

被引:3
作者
Hu, Lin [1 ]
He, Long [1 ]
Wang, Guanghua [2 ]
机构
[1] China Univ Min & Technol, Sch Chem Engn & Technol, Key Lab Coal Proc & Efficient Utilizat, Minist Educ, Xuzhou, Jiangsu, Peoples R China
[2] Wuhan Univ Sci & Technol, Sch Chem & Chem Engn, Hubei Coal Convers & New Carbon Mat Key Lab, Wuhan, Hubei, Peoples R China
关键词
Lignite; non-isothermal drying process; drying kinetics; diffusion coefficient; activation energy; COMBUSTION CHARACTERISTICS; PHYSICOCHEMICAL STRUCTURE; SHENGLI LIGNITE; MICROWAVE; PYROLYSIS; BEHAVIOR; WATER;
D O I
10.1080/15567036.2019.1587105
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
This study investigated the chemical functional groups' changes and drying kinetics characteristics of lignite during the non-isothermal drying process. Compared with the chemical functional groups' changes of raw lignite, chemical functional groups of lower bonding energy such as -OH, -COOH, C-O-C, and C-O, which was decreased in the dried lignite. Two periods of the non-isothermal drying in lignite were observed: the fast heating period and the falling rate period. With increasing heating rate of drying, the needed drying time of lignite decreased, but the drying rate of lignite increased during the non-isothermal drying process. With increasing heating rate, the effective diffusion coefficient values of lignite ranged from 1.08 x 10(-11) to 2.47 x 10(-11) m(2)/s. Two different kinetics models, iso-conversional Kissinger-Akahira-Sunose and Ozawa-Flynn-Wall models, were applied to calculate the drying kinetics parameters of lignite. The average activation energy of two models for non-isothermal drying process was 72.43 and 75.13 kJ/mol, respectively. The study can obtain the information on heat and mass transfer of lignite during the non-isothermal drying process.
引用
收藏
页码:586 / 596
页数:11
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