Pyrolysis of Lignocellulosic Biomass from Northeast China

The pyrolytic decomposition study of four species of lignocellulosic biomass (pine, poplar, bass and birch) from the Northeast China was carried out by thermogravimetric analysis (TGA) under the temperature range from 30 to 800 ℃ in the N2 atmosphere at four heating rates (β) of 10,20,40 and 60 ℃/min. The non-isothermal weight loss process of the above biomass samples was mainly composed of dehydration, rapid weight loss and slow weight loss, with the main pyrolysis reaction occurring in the temperature scope of 211~432 ℃. The temperature for the initialization of volatiles (Ts) and peak weight loss temperature(Tp)were between 211~273 ℃and 348~395 ℃, respectively. Peak weight loss rate (Rp) was in the scope of 340~2759μg﹒min-1. The apparent activation energy (E) and pre-exponential factor (A) were between 36.83~57.30 kJ/mol and 1.0×102 ~2.5×103 min-1, respectively. It was shown that Ts, Tp and R p got higher with the increase of β,Tp and Rp being positively proportional to β and almost exhibiting linearity. It can be concluded from the results that the reaction mechanism and process of biomass pyrolysis can be changed by the alteration of β.

[1]  Enrico Biagini,et al.  Devolatilization of Biomass Fuels and Biomass Components Studied by TG/FTIR Technique , 2006 .

[2]  G. Sakellaropoulos,et al.  Pyrolysis and Combustion Characteristics of Biomass and Waste-Derived Feedstock , 2006 .

[3]  D. T. Liang,et al.  Thermogravimetric Analysis−Fourier Transform Infrared Analysis of Palm Oil Waste Pyrolysis , 2004 .

[4]  L. Puigjaner,et al.  Further applications of a revisited summative model for kinetics of biomass pyrolysis , 2004 .

[5]  Panagiotis Grammelis,et al.  Thermogravimetric studies of the behavior of lignite–biomass blends during devolatilization , 2002 .

[6]  A. Demirbas,et al.  Biomass resource facilities and biomass conversion processing for fuels and chemicals , 2001 .

[7]  Ayhan Demirbas,et al.  Conversion of cotton cocoon shell to liquid products by pyrolysis , 2000 .

[8]  S. Şensöz,et al.  Influence of particle size on the pyrolysis of rapeseed (Brassica napus L.): fuel properties of bio-oil , 2000 .

[9]  Michael Jerry Antal,et al.  A Round-Robin Study of Cellulose Pyrolysis Kinetics by Thermogravimetry , 1999 .

[10]  D. Meier,et al.  State of the art of applied fast pyrolysis of lignocellulosic materials - a review , 1999 .

[11]  José L. Figueiredo,et al.  Pyrolysis kinetics of lignocellulosic materials—three independent reactions model , 1999 .

[12]  Michael A. Serio,et al.  TG-FTIR Study of the Influence of potassium Chloride on Wheat Straw Pyrolysis , 1998 .

[13]  Ayhan Demirbas,et al.  Biomass conversion processes , 1997 .

[14]  A. W. Coats,et al.  Kinetic Parameters from Thermogravimetric Data , 1964, Nature.