TG analysis and kinetic study of organic constituents in wastewater from coal-gasification process

被引:3
作者
Zhang, Wei [1 ]
Wang, Chang'an [1 ]
Li, Guangyu [1 ]
Liu, Yinhe [1 ]
Che, Defu [1 ]
机构
[1] Xi An Jiao Tong Univ, Sch Energy & Power Engn, State Key Lab Multiphase Flow Power Engn, Xian 710049, Peoples R China
基金
中国国家自然科学基金;
关键词
CGW; organic constituents; solids conversion; degradation rate; THERMOGRAVIMETRIC ANALYSIS; PYROLYSIS CHARACTERISTICS; PULVERIZED-COAL; BIOMASS; COMBUSTION; MODEL; DEGRADATION; FTIR; BEHAVIOR; STRAW;
D O I
10.1002/apj.2083
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
In the paper, the thermal reactivity of organic constituents from coal-gasification wastewater is performed through physicochemical and thermogravimetric (TG) analysis. The effects of reaction atmosphere, oxygen concentration, heating rate, and final temperature on both solids conversion and degradation rate are experimentally studied. The results indicate that organic constituents mainly consist of aliphatic hydrocarbon, phenols, and ammonium, and so on. The thermal degradation of organic constituents in various atmospheres can be divided into four regions: 100-200, 200-300, 300-410, and 410-900 degrees C. The TG/DTG curves present considerable differences in the last region compared with that in the first three regions. In addition, the degradation rate shows a considerable increase and moves toward higher temperature region with heating rate. Furthermore, the kinetic parameters of organic constituents are analyzed by one multi-heating rate method. The calculated results show that apparent activation energy of organic constituents varies between 82.8 and 91.3 kJ mol(-1) under various reaction atmospheres. This information is potentially useful for the design and retrofitting of the large-scale equipment to recover industrial wastewater. (C) 2017 Curtin University of Technology and John Wiley & Sons, Ltd.
引用
收藏
页码:406 / 414
页数:9
相关论文
共 44 条
[1]  
Alzueta MU, 2000, INT J CHEM KINET, V32, P498, DOI 10.1002/1097-4601(2000)32:8<498::AID-KIN8>3.0.CO
[2]  
2-H
[3]   Computational aspects of kinetic analysis Part A: The ICTAC kinetics project-data, methods and results [J].
Brown, ME ;
Maciejewski, M ;
Vyazovkin, S ;
Nomen, R ;
Sempere, J ;
Burnham, A ;
Opfermann, J ;
Strey, R ;
Anderson, HL ;
Kemmler, A ;
Keuleers, R ;
Janssens, J ;
Desseyn, HO ;
Li, CR ;
Tang, TB ;
Roduit, B ;
Malek, J ;
Mitsuhashi, T .
THERMOCHIMICA ACTA, 2000, 355 (1-2) :125-143
[4]   A review on anaerobic-aerobic treatment of industrial and municipal wastewater [J].
Chan, Yi Jing ;
Chong, Mei Fong ;
Law, Chung Lim ;
Hassell, D. G. .
CHEMICAL ENGINEERING JOURNAL, 2009, 155 (1-2) :1-18
[5]   The influence of pressure and temperature on coal pyrolysis/gasification [J].
Chen, Hanping ;
Yang, Haiping ;
Ju, Fudong ;
Wang, Jing ;
Zhang, Shihong .
ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, 2007, 2 (03) :203-212
[6]   Kinetics of isothermal and non-isothermal degradation of cellulose: model-based and model-free methods [J].
Dahiya, Jai Bhagwan ;
Kumar, Krishan ;
Muller-Hagedorn, Matthias ;
Bockhorn, Henning .
POLYMER INTERNATIONAL, 2008, 57 (05) :722-729
[7]   TG-FTIR pyrolysis of coal and secondary biomass fuels:: Determination of pyrolysis kinetic parameters for main species and NOx precursors [J].
de Jong, W. ;
Di Nola, G. ;
Venneker, B. C. H. ;
Spliethoff, H. ;
Wojtowicz, M. A. .
FUEL, 2007, 86 (15) :2367-2376
[8]   A modified Arrhenius equation to predict the reaction rate constant of Anyuan pulverized-coal pyrolysis at different heating rates [J].
Du, Rui-Ling ;
Wu, Keng ;
Xu, Da-An ;
Chao, Chang-Yao ;
Zhang, Li ;
Du, Xiao-Dong .
FUEL PROCESSING TECHNOLOGY, 2016, 148 :295-301
[9]  
Gardiner WilliamC., 2000, GAS PHASE COMBUSTION
[10]   Thermal degradation of alkaline black liquor from straw. Thermogravimetric study [J].
Gea, G ;
Murillo, MB ;
Arauzo, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (19) :4714-4721