Study of the reaction mechanism for preparing powdered activated coke with SO2 adsorption capability via one-step rapid activation method under flue gas atmosphere
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Study of the reaction mechanism for preparing powdered activated coke with SO2 adsorption capability via one-step rapid activation method under flue gas atmosphere
Study of the reaction mechanism for preparing powdered activated coke with SO2 adsorption capability via one-step rapid activation method under flue gas atmosphere
中国化学工程学报(英文版)2024年65卷第1期 页码:158-168
Affiliations:
1. School of Environmental Science and Engineering, Shandong University,Qingdao,China,266237
2. Weihai Research Institute of Industrial Technology of Shandong University,Weihai,China,264209
3. School of Energy and Power Engineering, Shandong University,Jinan,China,250061
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纸质出版:2024
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Binxuan Zhou, Jingcai Chang, Jun Li, 等. Study of the reaction mechanism for preparing powdered activated coke with SO2 adsorption capability via one-step rapid activation method under flue gas atmosphere[J]. 中国化学工程学报(英文版), 2024,65(1):158-168.
adsorption capability
Binxuan Zhou, Jingcai Chang, Jun Li, 等. Study of the reaction mechanism for preparing powdered activated coke with SO2 adsorption capability via one-step rapid activation method under flue gas atmosphere[J]. 中国化学工程学报(英文版), 2024,65(1):158-168.DOI:
adsorption capabilityDOI:
Study of the reaction mechanism for preparing powdered activated coke with SO2 adsorption capability via one-step rapid activation method under flue gas atmosphere
the impact of different reaction times on the preparation of powdered activated carbon (PAC) using a one-step rapid activation method under flue gas atmosphere is investigated
and the underlying reaction mechanism is summarized. Results indicate that the reaction process of this method can be divided into three stages:stage I is the rapid release of volatiles and the rapid consumption of O
2
primarily occurring within a reaction time range of 0-0.5 s; stage II is mainly the continuous release and diffusion of volatiles
which is the carbonization and activation coupling reaction stage
and the carbonization process is the main in this stage. This stage mainly occurs at the reaction time range of 0.5-2.0 s when SL-coal is used as material
and that is 0.5-3.0 s when JJ-coal is used as material; stage III is mainly the activation stage
during which activated components diffuse to both the surface and interior of particles. This stage mainly involves the reaction stage of CO
2
and H
2
O (g) activation
and it mainly occurs at the reaction time range of 2.0-4.0 s when SL-coal is used as material
and that is 3.0-4.0 s when JJ-coal is used as material. Besides
the main function of the first two stages is to provide more diffusion channels and contact surfaces/activation sites for the diffusion and activation of the activated components in the third stage. Mastering the reaction mechanism would serve as a crucial reference and foundation for designing the structure
size of the reactor
and optimal positioning of the activator nozzle in PAC preparation.
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