Multiscale CFD-DEM model for the CO2 gasification reaction of carbon anode

Fuel ◽  
2021 ◽  
Vol 297 ◽  
pp. 120692
Author(s):  
Mohammad Kavand
Fuel ◽  
2014 ◽  
Vol 120 ◽  
pp. 130-140 ◽  
Author(s):  
Daehee Kim ◽  
Sangmin Choi ◽  
Christopher R. Shaddix ◽  
Manfred Geier

2012 ◽  
Vol 51 (42) ◽  
pp. 13619-13626 ◽  
Author(s):  
Hua Fei ◽  
Song Hu ◽  
Faen Shi ◽  
Yuanlin Li ◽  
Dahua Jiang ◽  
...  

2011 ◽  
Vol 6 (2) ◽  
pp. 278-288 ◽  
Author(s):  
Yoshiaki YAMAZAKI ◽  
Kenichi HIRAKI ◽  
Tetsuya KANAI ◽  
Xiaoqing ZHANG ◽  
Yohsuke MATSUSHITA ◽  
...  

Fuel ◽  
2016 ◽  
Vol 178 ◽  
pp. 93-102 ◽  
Author(s):  
F. Chevarin ◽  
K. Azari ◽  
L. Lemieux ◽  
D. Ziegler ◽  
M. Fafard ◽  
...  

2013 ◽  
Vol 316-317 ◽  
pp. 153-156
Author(s):  
Tao Jun Lu ◽  
Yong Fa Zhang

The residue of Inner Mongolia lignite semi-coke by different final temperature hydrogenation system methane of CO2 gasification reactivity is studied by means of thermo gravimetric and X-Ray Diffraction method. The results show that, with the rise of hydrogasification temperature, the residue aromaticity fa increase, the residual carbon microcrystalline tend to graphitization, CO2 reactivity decrease and residue CO2 reaction temperature raise. The final hydrogenation temperature residue CO2 gasification reaction conversion rate curves similar and curve to temperature increase in the direction of movement.


2011 ◽  
Vol 33 (2) ◽  
pp. 1699-1706 ◽  
Author(s):  
Ethan S. Hecht ◽  
Christopher R. Shaddix ◽  
Alejandro Molina ◽  
Brian S. Haynes

1992 ◽  
Vol 71 (6) ◽  
pp. 428-435
Author(s):  
Tatsumi NISHIJIMA ◽  
Hideki ISSHIKI ◽  
Shiying LIN ◽  
Yoshihiko NINOMIYA ◽  
Mitsuho HIRATO ◽  
...  

2012 ◽  
Vol 550-553 ◽  
pp. 2754-2757
Author(s):  
Li Hong Zhao ◽  
Xi Jie Chu ◽  
Shao Juan Cheng

The CO2 gasification of three coal chars were investigated for determining the gasification reactivity and the kinetic parameters. Experiments were conducted in a fluidized-bed reactor at temperature of 1173 k, 1273 k and 1373 k at atmospheric pressure. Gasification kinetic parameters of the samples were determined using Homogeneous model and shrinking-core model. It is found that the gasification reaction under chemical-reaction-rate control, the gasification reactivity of coal char are strongly dependent on the rank of coals and gasification temperature. Both models could describe CO2 gasification equally well, these kinetic values are comparable with the reported in the literature for the other chars under chemical control conditions.


2016 ◽  
Vol 30 (7) ◽  
pp. 3275-3281 ◽  
Author(s):  
Tahereh Jalalabadi ◽  
Chengguo Li ◽  
Hakgyu Yi ◽  
Donggeun Lee

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