The use of electrical resistance tomography for the characterization of gas holdup inside a bubble column bioreactor containing activated sludge

被引:43
作者
Babaei, Roghayyeh [1 ]
Bonakdarpour, Babak [1 ]
Ein-Mozaffari, Farhad [2 ]
机构
[1] Amirkabir Univ Technol, Dept Chem Engn, Tehran, Iran
[2] Ryerson Univ, Dept Chem Engn, Toronto, ON, Canada
关键词
Electrical resistance tomography; Activated sludge; Bobble column bioreactors; Gas holdup; Sludge rheology; Mixed Liquor Suspended Solids; COMPUTATIONAL FLUID-DYNAMICS; SUBMERGED MEMBRANE BIOREACTORS; HYDRAULIC RETENTION TIME; WASTE-WATER TREATMENT; MASS-TRANSFER; OXYGEN-TRANSFER; AERATION TANKS; HEAT-TRANSFER; HYDRODYNAMICS; REACTORS;
D O I
10.1016/j.cej.2015.01.042
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Gas holdup is a determinant factor regarding the efficiency of the activated sludge processes. Despite the numerous studies on the characterization of gas holdup in two or three phase systems, lack of experimental data in systems including actual cells as the solid phase has been emphasized in the literature. This study is a response to the need for an appropriate knowledge on the gas holdup behavior in the real activated sludge systems. The capabilities of electrical resistance tomography in performing local and global measurements in a non-intrusive manner made it possible to examine the influence of MISS concentration and aeration intensity on the overall as well as spatial distribution of gas holdup within the activated sludge bioreactor. In order to cover all activated sludge processes, a wide range of MISS concentration (0.712-15.86 g/L) was employed, and the effect of MISS on rheological characteristics of the corresponding mixed liquor was measured and modeled. The results of the present study revealed an initially increasing followed by decreasing variation of overall gas holdup with increasing MLSS concentration which is reported in this paper for the first time. Radial distribution of gas holdup was also modeled and the variations of central, wall, and cross sectional average gas holdups with axial location, MLSS, and air velocity were specified. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:260 / 269
页数:10
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