Kinetic study of the pyrolysis of miscanthus and its acid hydrolysis residue by thermogravimetric analysis

被引:81
作者
Cortes, Ana Maria [1 ]
Bridgwater, A. V. [1 ]
机构
[1] Aston Univ, Bioenergy Res Grp, European Bioenergy Res Inst, Birmingham B4 7ET, W Midlands, England
关键词
Kinetics; Acid hydrolysis residue; Thermogravimetric analysis; Activation energy; Pre-exponential factor; Isoconversional methods; CATALYZED HYDROLYSIS; ACTIVATION-ENERGY; WHEAT-STRAW; BY-PRODUCTS; BIO-OIL; BIOMASS; COMBUSTION; LIGNIN; TGA; HEMICELLULOSE;
D O I
10.1016/j.fuproc.2015.05.013
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
The kinetic parameters of the pyrolysis of miscanthus and its acid hydrolysis residue (AHR) were determined using thermogravimetric analysis (TGA). The AHR was produced at the University of Limerick by treating miscanthus with 5 wt.% sulphuric acid at 175 degrees C as representative of a lignocellulosic acid hydrolysis product. For the TGA experiments, 3 to 6 g of sample, milled and sieved to a particle size below 250 mu m, were placed in the TGA ceramic crucible. The experiments were carried out under non-isothermal conditions heating the samples from 50 to 900 degrees C at heating rates of 2.5, 5, 10, 17 and 25 degrees C/min. The activation energy (E-A) of the decomposition process was determined from the TGA data by differential analysis (Friedman) and three isoconversional methods of integral analysis (Kissinger-Akahira-Sunose, Ozawa-Flynn-Wall, Vyazovkin). The activation energy ranged from 129 to 156 kJ/mol for miscanthus and from 200 to 376 kJ/mol for AHR increasing with increasing conversion. The reaction model was selected using the non-linear least squares method and the pre-exponential factor was calculated from the Arrhenius approximation. The results showed that the best fitting reaction model was the third order reaction for both feedstocks. The pre-exponential factor was in the range of 5.6 x 10(10) to 3.9 x 10(+13) min(-1) for miscanthus and 2.1 x 10(16) to 7.7 x 10(25) min(-1) for AHR. (C) 2015 The Authors. Published by Elsevier B.V.
引用
收藏
页码:184 / 193
页数:10
相关论文
共 64 条
[1]   Pyrolysis kinetics of forestry residues from the Portuguese Central Inland Region [J].
Amutio, Maider ;
Lopez, Gartzen ;
Alvarez, Jon ;
Moreira, Rui ;
Duarte, Gustavo ;
Nunes, Joao ;
Olazar, Martin ;
Bilbao, Javier .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2013, 91 (12) :2682-2690
[2]  
ASTM, 2003, STAND TEST METH COMP
[3]  
ASTM, 2001, STAND TEST METH ASH
[4]  
ASTM, 2007, ASTM E119-07, P1
[5]   KINETIC-ANALYSIS OF LIGNIN PYROLYSIS USING NON-ISOTHERMAL TGA DATA [J].
AVNI, E ;
COUGHLIN, RW .
THERMOCHIMICA ACTA, 1985, 90 (AUG) :157-167
[6]  
Banks Scott., 2014, Ash control methods to limit biomass inorganic content and its effect on fast pyrolysis bio-oil stability
[7]   Fast pyrolysis of Miscanthus sinensis in fluidized bed reactors: Characteristics of product yields and biocrude oil quality [J].
Bok, Jin Pil ;
Choi, Hang Seok ;
Choi, Joon Weon ;
Choi, Yeon Seok .
ENERGY, 2013, 60 :44-52
[8]  
Bridgwater A.V., 1999, FAST PYROLYSIS BIOMA, V1
[9]   Miscanthus: a fast-growing crop for biofuels and chemicals production [J].
Brosse, Nicolas ;
Dufour, Anthony ;
Meng, Xianzhi ;
Sun, Qining ;
Ragauskas, Arthur .
BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR, 2012, 6 (05) :580-598
[10]   Some methodological problems concerning nonisothermal kinetic analysis of heterogeneous solid-gas reactions [J].
Budrugeac, P ;
Segal, E .
INTERNATIONAL JOURNAL OF CHEMICAL KINETICS, 2001, 33 (10) :564-573