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
Link To Document :
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