Physicochemical structure characteristics and combustion kinetics of low-rank coal by hydrothermal carbonization

Energy ◽  
2021 ◽  
pp. 121682
Author(s):  
Nan Zhang ◽  
Guangwei Wang ◽  
Chunmei Yu ◽  
Jianliang Zhang ◽  
Han Dang ◽  
...  
RSC Advances ◽  
2018 ◽  
Vol 8 (41) ◽  
pp. 22909-22916 ◽  
Author(s):  
Yingjie Hu ◽  
Zhiqiang Wang ◽  
Xingxing Cheng ◽  
Chunyuan Ma

The combustion reaction kinetics of pyrolytic char of low-rank coal was investigated by using thermal analysis technology.


2019 ◽  
Vol 1242 ◽  
pp. 012053
Author(s):  
A Rahim ◽  
S S Surjono ◽  
D H Amijaya ◽  
K Sasaki

ACS Omega ◽  
2021 ◽  
Vol 6 (39) ◽  
pp. 25772-25781
Author(s):  
Han Dang ◽  
Guangwei Wang ◽  
Chunmei Yu ◽  
Xiaojun Ning ◽  
Jianliang Zhang ◽  
...  

2016 ◽  
Vol 205 ◽  
pp. 199-204 ◽  
Author(s):  
Wei Yang ◽  
Hui Wang ◽  
Meng Zhang ◽  
Jiayu Zhu ◽  
Jie Zhou ◽  
...  

2009 ◽  
Vol 25 (12) ◽  
pp. 2597-2603 ◽  
Author(s):  
LI Mei-Fen ◽  
◽  
ZENG Fan-Gui ◽  
SUN Bei-Lei ◽  
QI Fu-Hui

2018 ◽  
Vol 91 (2) ◽  
pp. 311-322 ◽  
Author(s):  
Berrin Engin ◽  
Hüsnü Atakül

Author(s):  
A. T. Harris ◽  
S. A. Scott ◽  
J. S. Dennis ◽  
A. N. Hayhurst ◽  
J. F. Davidson

This paper gives the first measurements from a project investigating the gasification of dried sewage sludge in a laboratory scale, bubbling fluidized bed at atmospheric pressure. The aim of the work was to examine the reactions occurring in a fluidized bed gasifier rather than simply treat the reactor as a ‘black box’. Experiments were performed to investigate the rates of drying, devolatilisation, gasification and combustion. Thermogravimetric analysis, as well as batch fluidized bed experiments using mechanically dewatered, dried and pelletised municipal sewage sludges from different regions in the UK were performed. A comparison was made between the different samples of sludge and a low rank coal and softwood biomass. A distributed activation energy model (DAEM) for interpreting the kinetics of devolatilisation was also investigated. The model was able to reduce the results from several TGA experiments to a single curve characterised by a single parameter, the pre-exponential factor, A.


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