Effect of particle size on thermal decomposition and devolatilization kinetics of melon seed shell

被引:16
作者
Ahmed, Awwal [1 ]
Afolabi, Eyitayo Amos [1 ]
Garba, Mohammed Umar [1 ]
Musa, Umaru [1 ]
Alhassan, Mohammed [1 ]
Ishaq, Kariim [1 ]
机构
[1] Fed Univ Technol, Chem Engn Dept, Minna, Nigeria
关键词
Activation energy; Biofuel; Decomposition; Kinetics; Melon seed shell; Pyrolysis; SUGAR-CANE BAGASSE; THERMOGRAVIMETRIC ANALYSIS; COMBUSTION CHARACTERISTICS; HEATING RATE; BIOMASS PYROLYSIS; CO-PYROLYSIS; TEMPERATURE; PARAMETERS; NITROGEN; ENERGY;
D O I
10.1080/00986445.2018.1555530
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Thermogravimetric analysis (TGA) and devolatilization kinetics of melon seed shell (MSS) at different particle sizes (150 mu m and 500 mu m) and at different heating rates (10, 15, 20, and 25 degrees C/min) were investigated with the aid of TGA. The results of the TGA analysis show that the TGA curves corresponding to the first and third stages for 150 mu m particle sizes exhibited some bumps that developed at the first and third stages of pyrolysis. It was also observed that at constant heating rate, the maximum peak temperature increases as the particle sizes increase from 150 to 500 mu m, whereas 500 mu m particle sizes exhibited higher peak temperatures compared to 150 mu m particle sizes. The resulting TGA data were applied to the Kissinger (K), Kissinger-Akahira-Sunose (KAS) and Flynn-Wall-Ozawa (FWO) methods and kinetic parameters (activation energy, E and frequency factor, A) were determined. The E and A obtained using K method were 74.27kJ mol(-1) and 3.84x10(5)min(-1) for 150 mu m particle size, whereas for 500 mu m particle size were 97.12kJ mol(-1) and 3.74x10(7)min(-1), respectively. However, the average E and A obtained using KAS and FWO methods were 82.35kJ mol(-1), 1.29x10(7)min(-1), and 88.50kJ mol(-1), 1.32x10(7)min(-1) for 150 mu m particle sizes. While for 500 mu m particle sizes, the E and A were 108.46kJ mol(-1), 3.14x10(9)min(-1), and 113.05kJ mol(-1), 7.56x10(9)min(-1), respectively. It was observed that E and A calculated from FWO and KAS methods were very close and higher than that obtained by K method. It was observed that the minimum heat required for the cracking of MSS particles into products is reached later at higher peak temperatures since the heat transfer is less effective as they are at lower peak temperatures.
引用
收藏
页码:1228 / 1240
页数:13
相关论文
共 54 条
[1]   Comparative investigation for the determination of kinetic parameters for biomass pyrolysis by thermogravimetric analysis [J].
Abdelouahed, Lokmane ;
Leveneur, Sebastien ;
Vernieres-Hassimi, Lamiae ;
Balland, Laurent ;
Taouk, Bechara .
JOURNAL OF THERMAL ANALYSIS AND CALORIMETRY, 2017, 129 (02) :1201-1213
[2]   Effect of particle size and heating rate on the pyrolysis of Silopi asphaltite [J].
Altun, NE ;
Hicyilmaz, C ;
Kök, MV .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2003, 67 (02) :369-379
[3]  
Bande Y. M., 2012, International Journal of Agricultural Research, V7, P494, DOI 10.3923/ijar.2012.494.499
[4]   Pyrolysis of pellets made with biomass and glycerol: Kinetic analysis and evolved gas analysis [J].
Bartocci, P. ;
Anca-Couce, A. ;
Slopiecka, K. ;
Nefkens, S. ;
Evic, N. ;
Retschitzegger, S. ;
Barbanera, M. ;
Buratti, C. ;
Cotana, F. ;
Bidini, G. ;
Fantozzi, F. .
BIOMASS & BIOENERGY, 2017, 97 :11-19
[5]  
Basu P, 2010, BIOMASS GASIFICATION AND PYROLYSIS: PRACTICAL DESIGN AND THEORY, P1
[6]   Physical - Chemical Characterization of Biomass Samples for Application in Pyrolysis Process [J].
Braz, Carlos Eduardo M. ;
Crnkovic, Paula M. .
ICONBM: INTERNATIONAL CONFERENCE ON BIOMASS, PTS 1 AND 2, 2014, 37 :523-528
[7]   Thermogravimetric analysis and kinetics of coal/plastic blends during co-pyrolysis in nitrogen atmosphere [J].
Cai, Junqing ;
Wang, Yiping ;
Zhou, Limin ;
Huang, Qunwu .
FUEL PROCESSING TECHNOLOGY, 2008, 89 (01) :21-27
[8]   Pyrolysis kinetics of hazelnut husk using thermogravimetric analysis [J].
Ceylan, Selim ;
Topcu, Yildiray .
BIORESOURCE TECHNOLOGY, 2014, 156 :182-188
[9]   Effects of temperature and particle size on bio-char yield from pyrolysis of agricultural residues [J].
Demirbas, A .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 2004, 72 (02) :243-248
[10]   An experimental and kinetic modeling study of glycerol pyrolysis [J].
Fantozzi, F. ;
Frassoldati, A. ;
Bartocci, P. ;
Cinti, G. ;
Quagliarini, F. ;
Bidini, G. ;
Ranzi, E. M. .
APPLIED ENERGY, 2016, 184 :68-76