Effects of Biomass Particle Size on Slow Pyrolysis Kinetics and Fast Pyrolysis Product Distribution

2017 ◽  
Vol 9 (3) ◽  
pp. 465-477 ◽  
Author(s):  
Dadi V. Suriapparao ◽  
R. Vinu
Materials ◽  
2020 ◽  
Vol 13 (14) ◽  
pp. 3188
Author(s):  
Paweł Kazimierski ◽  
Paulina Hercel ◽  
Katarzyna Januszewicz ◽  
Dariusz Kardaś

The aim of this study was to assess the possibility of using furniture waste for smokeless fuel production using the pyrolysis process. Four types of wood-based wastes were used in the pyrolysis process: pine sawdust (PS), chipboard (CB), medium-density fiberboard (MDF), and oriented strand board (OSB). Additionally, the slow and fast types of pyrolysis were compared, where the heating rates were 15 °C/min and 100 °C/min, respectively. Chemical analyses of the raw materials and the pyrolysis product yields are presented. A significant calorific value rise was observed for the solid pyrolysis products (from approximately 17.5 MJ/kg for raw materials up to approximately 29 MJ/kg for slow pyrolysis products and 31 MJ/kg for fast pyrolysis products). A higher carbon content of char was observed in raw materials (from approximately 48% for raw materials up to approximately 75% for slow pyrolysis products and approximately 82% for fast pyrolysis products) than after the pyrolysis process. This work presents the possibility of utilizing waste furniture material that is mostly composed of wood, but is not commonly used as a substrate for conversion into low-emission fuel. The results prove that the proposed solution produced char characterized by the appropriate properties to be classified as smokeless coal.


Author(s):  
Theodoros Damartzis ◽  
Margaritis Kostoglou ◽  
Anastasia Zabaniotou

In the present study, a model for the fast pyrolysis of a spherical biomass particle has been developed. The model admits the generation of data which are not accessible experimentally such as the intra-particle temperature and concentration distribution. Simulations have been carried using data from the reactor as well as from literature and the effects of the heating rate and the particle size have been examined. The kinetic model is coupled with a heat transfer model. The reaction kinetic constants have been chosen in order to match the theory to the data taken from experiments carried out in a laboratory wire mesh reactor, for a temperature range from 573 K to 873 K and a heating rate of 200 K/s. Pyrolysis temperature and product distribution profiles in both spatial and temporal directions throughout the particle are presented. The effects of the particle size and the reactor's heating rate in the final pyrolysis products and temperature are shown and discussed. Simulations were carried out using Matlab and the model has been validated against the experimental results. The heating rate, which is an important operating condition in thermal processes, seems to have a positive effect on the biomass conversion to gaseous and liquid products, an increase of the first resulting to an increase of the second. Particle size was found to have a negative effect on pyrolysis conversion as larger particles tend to give higher char yields. For the particular experimental system analyzed here, it seems that the radial non-uniformity is not very large and acceptable results can also be taken using a lumped particle model. Validation of the model with experimental data showed great accordance, thus the model could be used for the prediction of final pyrolysis yields and temperatures.


Author(s):  
Lijie Cui ◽  
Jianzhong Yao ◽  
Weigang Lin ◽  
Zheng Zhang

The flash pyrolysis of Huolinhe coal was carried out in a fast-entrained bed reactor. The investigation focuses on the effects of pyrolysis temperature and particle size on pyrolysis product distributions and gas and liquid compositions. Increasing temperature results in an increase of the gaseous product. There is an optimum temperature on the maximum liquid yield, which is around 650°C. An increase in particle size leads to a decrease of liquid products. Some amount of phenol group was found in the liquid products, which may produce the chemicals with high value. The results provide fundamental data and optimal conditions to maximize light oils yields for the coal topping process.


2014 ◽  
Vol 169 ◽  
pp. 812-815 ◽  
Author(s):  
Tipeng Wang ◽  
Xiaoning Ye ◽  
Jun Yin ◽  
Zaixing Jin ◽  
Qiang Lu ◽  
...  

2021 ◽  
Vol 49 (11) ◽  
pp. 1638-1647
Author(s):  
Jie-han ZHANG ◽  
Guo-jun KANG ◽  
Hang YANG ◽  
Zhou-en LIU ◽  
Jian YU ◽  
...  

2017 ◽  
Vol 13 (4) ◽  
pp. 55-63 ◽  
Author(s):  
Yeonseok Choi ◽  
Sangkyu Choi ◽  
Seockjoon Kim ◽  
Soyoung Han ◽  
Yeonwoo Jeong

2021 ◽  
Vol 1051 (1) ◽  
pp. 012075
Author(s):  
H Tan ◽  
C T Lee ◽  
P Y Ong ◽  
K Y Wong ◽  
C P C Bong ◽  
...  

2019 ◽  
Vol 132 ◽  
pp. 486-496 ◽  
Author(s):  
Bo Wang ◽  
Fanfan Xu ◽  
Peijie Zong ◽  
Jinhong Zhang ◽  
Yuanyu Tian ◽  
...  

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