The motion mechanism and characteristic of bubble in a pseudo-2D tapered fluidized bed
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The motion mechanism and characteristic of bubble in a pseudo-2D tapered fluidized bed
The motion mechanism and characteristic of bubble in a pseudo-2D tapered fluidized bed
中国化学工程学报(英文版)2022年46卷第6期 页码:255-270
Affiliations:
1. Shandong Engineering Laboratory for Preparation and Application of High-performance Carbon-Materials, College of Electromechanical Engineering, Qingdao University of Science and Technology,Shandong,China,266061
Wenjuan Bai, Dianming Chu, Kuanxin Tang, 等. The motion mechanism and characteristic of bubble in a pseudo-2D tapered fluidized bed[J]. 中国化学工程学报(英文版), 2022,46(6):255-270.
Wenjuan Bai, Dianming Chu, Kuanxin Tang, Lei Geng, Yan Li, Yan He. The motion mechanism and characteristic of bubble in a pseudo-2D tapered fluidized bed[J]. Chinese Journal of Chemical Engineering, 2022, 46(6): 255-270.
Wenjuan Bai, Dianming Chu, Kuanxin Tang, 等. The motion mechanism and characteristic of bubble in a pseudo-2D tapered fluidized bed[J]. 中国化学工程学报(英文版), 2022,46(6):255-270.DOI:
Wenjuan Bai, Dianming Chu, Kuanxin Tang, Lei Geng, Yan Li, Yan He. The motion mechanism and characteristic of bubble in a pseudo-2D tapered fluidized bed[J]. Chinese Journal of Chemical Engineering, 2022, 46(6): 255-270.DOI:
The motion mechanism and characteristic of bubble in a pseudo-2D tapered fluidized bed
V) were bed materials in the pseudo-2D tapered fluidized bed (TFB) with/without a distributor. A detailed investigation of the motion mechanism of bubbles was carried out. The high-speed photography and image analysis techniques were used to study bubble characteristic and mixing behavior in the tapered angle of TFB without a distributor. The fractal analysis method was used to analyze the degree of particles movement. Results showed that an S-shaped motion trajectory of bubbles was captured in the bed of
@
V particles. The population of observational bubbles in the bed of
@
V particles was more than that of
@
A particles
and the bubble size was smaller in the bed of
@
V particles than that of
@
A particles. The motion mechanism of bubbles had been shown to be related to bed materials and initial bed height in terms of analysis and comparison of bubble diameter
bubble aspect ratio and bubble shape factor. Importantly
compared to the TFB with a distributor
the TFB without a distributor had been proved to be beneficial to the CNT fluidization according to the study of bubble characteristic and the degree of the particle movement. Additionally
it was found that the mixing behavior of
@
V particles was better than
@
A particles in the tapered angle of TFB without a distributor.
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