DocumentCode
537202
Title
Research on the Mass Transfer Dynamics of Biologic Fluidized Bed
Author
Chen Yue-fang ; Yu Lu-lu ; Liu Hui
Author_Institution
Dept. of Environ. Eng., Univ. of Sci. & Technol. Beijing, Beijing, China
fYear
2010
fDate
7-9 Nov. 2010
Firstpage
1
Lastpage
4
Abstract
In order to exert the advantages of biologic fluidized bed best and optimizing the working parameters of the fluidized bed, research has been done on the mass transfer dynamics of the biologic fluidized bed. It proved that the cylindrical fluidized bed had the best fluidization effect and low dissipation of energy. There is a linear growth relation between the aeration intensity and the ratio of the stuffing; the movement velocity of the stuffing increases significantly as the aeration quantity grows; the movement velocity of the stuffing falls as the ratio of the stuffing decreases. According to the influence that the ratio of the stuffing and the aeration quantity have on the oxygen transfer coefficient (KLa), oxygen transfer rate (dc/dt) and the oxygenation capacity (OC) of the reactor, considering the economical efficiency simultaneously, the conclusion is that the fluidized bed has the best fluidization effect and highest oxygen transfer ratio when the aeration quantity is 0.20m3/h and the stuffing ratio is 30%.
Keywords
biotechnology; fluidisation; fluidised beds; mass transfer; aeration intensity; biologic fluidized bed; cylindrical fluidized bed; fluidization effect; mass transfer dynamics; oxygen transfer coefficient; oxygen transfer rate; oxygenation capacity; stuffing ratio; Biology; Fluid dynamics; Fluidization; Hydrodynamics; Inductors; Oxygen; Wastewater treatment;
fLanguage
English
Publisher
ieee
Conference_Titel
E-Product E-Service and E-Entertainment (ICEEE), 2010 International Conference on
Conference_Location
Henan
Print_ISBN
978-1-4244-7159-1
Type
conf
DOI
10.1109/ICEEE.2010.5661143
Filename
5661143
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