Dynamics of trace elements release in a coal pyrolysis process☆

Fuel ◽  
2003 ◽  
Vol 82 (10) ◽  
pp. 1281-1290 ◽  
Author(s):  
Elwira Zajusz-Zubek ◽  
Jan Konieczyński
2002 ◽  
Vol 77-78 ◽  
pp. 137-143 ◽  
Author(s):  
Ruixia Guo ◽  
Jianli Yang ◽  
Dongyan Liu ◽  
Zhenyu Liu

2013 ◽  
Vol 860-863 ◽  
pp. 518-521
Author(s):  
Jia Qun Xia ◽  
Hu Ping Li

To find out the Co-pyrolysis characteristics of Dianchi Lake sludge and coal,Dianchi Lake sludge was introduced into coal pyrolysis process. In this paper,the pyrolysis experiments of Dianchi Lake sludge and coal were carried out by TG and TGA. Results show that the TG and DTG profiles of Dianchi Lake sludge were similar to coal, but different from coal under various blending ratios.Interaction was observed between the solid phases of Dianchi Lake sludge. The results provide a reference for further study on co-pyrolysis of Dianchi Lake sludge and coal to a certain extent.


2012 ◽  
Vol 557-559 ◽  
pp. 2189-2196
Author(s):  
Hui Feng Yuan ◽  
De Min He ◽  
Jun Guan ◽  
Qiu Min Zhang

Simulation and study on Texaco gasification of semi-cokes prepared by DG coal pyrolysis process has been carried out by using Aspen Plus. The possibility that pyrolytic semi-cokes is used as the raw materials is discussed. Sensitivity study runs are performed to analyze the effects of oxygen-to-char mass ratio, mass percentage of char in char water slurry and gasification pressure on the gasification process. Simulations indicate that molar percent content of effective components (CO+H2) reaches as high as 67.94% under operational conditions which oxygen-to-char mass ratio is 0.75; char water slurry concentration is 62.5% and gasification pressure is 4.0MPa. So semi-cokes made by DG coal pyrolysis process is the excellent raw materials for gasification. Sensitivity analysis show that oxygen-to-char mass ratio and mass percentage of char in char water slurry are the main factors that affect the gasification process; gasification pressure has little effect on the results of char gasification.


Fuel ◽  
2022 ◽  
Vol 308 ◽  
pp. 121929
Author(s):  
Xiaohe Xiong ◽  
Yang Miao ◽  
Xuchao Lu ◽  
Houzhang Tan ◽  
Zia ur Rahman ◽  
...  

Energies ◽  
2020 ◽  
Vol 13 (9) ◽  
pp. 2352
Author(s):  
Tianxu Shen ◽  
Jiang Zhang ◽  
Laihong Shen ◽  
Lei Bai ◽  
Jingchun Yan

The frequent outbreak of cyanobacteria bloom results in an urgent need for the resource utilization of cyanobacteria. However, the development of routine thermal treatment (i.e., gasification and pyrolysis) is hindered by the issue of high moisture content. In order to minimize the dewatering requirement, this study investigated the chemical looping co-gasification of the cyanobacteria/coal mixture. The results showed that the residual moisture of cyanobacteria not only could serve as the gasifying agent of coal, but also presented a better gasification effect than the injecting steam. Meanwhile, blending cyanobacteria also improved the performance of coal chemical looping gasification in terms of the syngas quality, gasification rate, and carbon conversion efficiency. Cyanobacteria pyrolysis supplied abundant hydrocarbons and hydrogen-rich gases. The highest syngas yield of 1.26 Nm3/kg was obtained in the mixture fuel of 46 wt.% cyanobacteria and 54 wt.% coal under a 0.3 oxygen carrier-to-fuel ratio. A slight interaction effect was observed in the pyrolysis process, in which the reactivity of coal pyrolysis was enhanced by the oxygenated groups of cyanobacteria volatile. The dominant motive of the interaction effect was the catalytic effect of alkali metals of cyanobacteria ash on the coal gasification. However, the formation of aluminosilicates deactivated alkali metals and further inhibited the char gasification. The intensity of interaction effect was demonstrated to be highly relevant with the (Na + K)/Al molar ratio of ash. The most prominent interaction effect occurred for the sample with 82 wt.% cyanobacteria, but a negative interaction was observed in the sample with 10 wt.% cyanobacteria. Both homogeneous reaction and shrinking core models showed the excellent fitting performance in the char gasification process. However, these two models could not be applied to the initial pyrolysis process because of the intricate mechanisms.


2020 ◽  
Vol 200 ◽  
pp. 106269 ◽  
Author(s):  
Tao Wang ◽  
Cheng Li ◽  
Binxuan Zhou ◽  
Yi Zhang ◽  
Man Zhang ◽  
...  

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