Flocculation parameter and fractal dimension model in a conical fluidized bed
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Flocculation parameter and fractal dimension model in a conical fluidized bed
CIESC JournalIssue 5, Pages: 1262-1267(2010)
作者机构:
1. 吉林大学环境与资源学院
2. 同济大学环境科学与工程学院
3. 中国市政工程东北设计研究院
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Online First:05 May 2010,
Published:05 May 2010
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WANG Ting, ZHOU Dandan, DONG Shuangshi, et al. Flocculation parameter and fractal dimension model in a conical fluidized bed[J]. CIESC Journal, 2010, (5): 1262-1267.
DOI:
WANG Ting, ZHOU Dandan, DONG Shuangshi, et al. Flocculation parameter and fractal dimension model in a conical fluidized bed[J]. CIESC Journal, 2010, (5): 1262-1267.DOI:
Flocculation parameter and fractal dimension model in a conical fluidized bed
Micro-vortex in liquid phase of conical fluidized-bed flocculation reactor
caused by fluidizing solid particles
was utilized to make colloids collision and aggregation
which results in the formation of flocs.When the value of GT increased from 1836.51 to 5399.53
the removal fraction (RF) of kaolin clay suspension increased from 23.97% to 85.37%.Also
The RF increased with the decreasing of G and the increasing of T
when G was within 169.2—189.7 s-1.According to the Fractal Dimension model
the correlation coefficient of flocs was above 0.9 at the similar operation conditions of reactor.This indicated the similarity of the flocs properties
which led to a narrow distribution of free falling velocity
and the maximum value of amount of flocs particles with the same falling velocity was up to 45%.