Characterization of dynamic behavior in the liquid spray zone of a bottom-spouted fluidized bed
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Characterization of dynamic behavior in the liquid spray zone of a bottom-spouted fluidized bed
Chinese Journal of Chemical EngineeringVol. 95, Issue 7, Pages: 194-206(2026)
Affiliations:
Laboratory of Green & Smart Chemical Engineering in Universities of Shandong, College of Chemical Engineering, Qingdao University of Science and Technology, Qingdao 266042, China
Center of Carbon Capture and Industrial Utilization, Jiangmen Laboratory of Carbon Science and Technology, Jiangmen 529020, China
College of Health Science and Environmental Engineering, Shenzhen Technology University, Shenzhen 518118, China
Sun Chengbin, Wang Meng, Zhan Dekang, et al. Characterization of dynamic behavior in the liquid spray zone of a bottom-spouted fluidized bed[J]. Chinese Journal of Chemical Engineering, 2026, 95(7): 194-206.
DOI:
Sun Chengbin, Wang Meng, Zhan Dekang, et al. Characterization of dynamic behavior in the liquid spray zone of a bottom-spouted fluidized bed[J]. Chinese Journal of Chemical Engineering, 2026, 95(7): 194-206.DOI:
Characterization of dynamic behavior in the liquid spray zone of a bottom-spouted fluidized bed
The dynamic behavior and particle shape effects in the liquid spray zone were investigated through temperature standard deviation
liquid—solid contact efficiency
and electrical conductivity signals. Results indicate that temperature standard deviation increases with proximity to the nozzle. Elevated atomisation gas velocity (
U
L
) reduces droplet diameter and improves their dispersion
which leads to a more uniform temperature distribution and a resulting decrease in standard deviation. The temperature standard deviation is decreased and then increased with the increasing of fluidized gas velocity (
U
f
). Non-spherical particles had a higher temperature standard deviation than spherical particles. This resulted from particle agglomeration
where lower sphericity led to stronger fluctuations. The liquid—solid contact efficiency is enhanced with the increasing of spouted gas velocity (
U
s
)
U
L
and
U
f
all. As the liquid spouted rate (
Q
L
) increased
the liquid—solid contact efficiency
determined by particle capture of droplets
first rose and then declined. Non-spherical particles exhibit higher liquid—solid contact efficiency than that of spherical particles due to longer residence times
and larger contact areas with droplets. Droplet fluctuations are intense near the nozzle
resulting in high electrical conductivity signal intensity. Increased
U
s
enhances airflow effects
causing frequent voltage signal fluctuations. Flake-like particles accumulate more droplets due to agglomeration
enabling droplets to reach higher bed positions. These studies provide promising research directions for the development of adsorbent pelletization in CO
2
capture.
关键词
Keywords
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