For numerical simulation of coal pyrolysis using the fragmentation and diffusionn (FD) model
a numerical method was proposed. The pyrolysis of three kinds of coal in a heated-tube reactor was simulated respectively
and the results were compared with the experimental results and also with the numerical results of FG-DVC model and CPD model. The effect of pyrolysis temperature and particle diameter on coal pyrolysis product was also studied. The accuracy of FD model was higher than FG-DVC model and CPD model
proving that FD model was more applicable for numerical simulation of coal pyrolysis. The gas product increased rapidly by increasing pyrolysis temperature until 1373 K
and then was nearly constant when pyrolysis temperature was higher than 1373 K. The tar product decreased with increasing pyrolysis temperature
and less time was needed to reach the maximum tar amount. The gas product and tar product both decreased by increasing particle diameter of coal
while more time was needed to reach the maximum tar amount.
Evaluation and application of pyrolysis kinetic model of Wucaiwan coal and Tulufan coal
Molecular model and pyrolysis simulation of Zaoquan coal
A kinetic model based on TGA data for pyrolysis of Zhundong coal
Study on capture reaction of free radicals in pyrolysis reaction based on Py-GC/MS
Synthesis of N-doped carbon micro-nanotubes using coal-based polyaniline as a carbon and nitrogen source
Related Author
Liping WEI
Guodong JIANG
Yukuan GU
Haipeng TENG
Wei FENG
Hongfeng GAO
Gui WANG
Langlang WU
Related Institution
College of Chemical Engineering, Northwestern University, Chemical Engineering Research Center of the Ministry of Education for Advanced Use Technology of Shanbei Energy, , Shaanxi
Northwest China Research Institute of Electronic Equipment, , Shaanxi
State Key Laboratory of High-efficiency Utilization of Coal and Green Chemical Engineering, College of Chemistry and Chemical Engineering, Ningxia University
College of Chemical Engineering, Northwest University, Chemical Engineering Research Center of Ministry of Education for Advanced Use Technology of Shanbei Energy
Department of Chemistry and Chemical Engineering, Xi’an University of Science & Technology