Experiment and calculation of filtration processes in an external-loop airlift ceramic membrane bioreactor

被引:17
|
作者
Zhang, Feng [1 ]
Jing, Wenheng [1 ]
Xing, Weihong [1 ]
Xu, Nanping [1 ]
机构
[1] Nanjing Univ Technol, Coll Chem & Chem Engn, State Key Lab Mat Oriented Chem Engn, Nanjing 210009, Peoples R China
基金
中国博士后科学基金; 中国国家自然科学基金;
关键词
Aeration; Ceramic membrane; Filtration; Hydrodynamics; Mathematical modelling; Turbulence; GAS-SPARGED ULTRAFILTRATION; HOLLOW-FIBER MEMBRANES; CROSS-FLOW MICROFILTRATION; WASTE-WATER TREATMENT; TUBULAR MEMBRANES; PERMEATE FLUX; SLUG FLOW; PERFORMANCE; PROMOTERS;
D O I
10.1016/j.ces.2009.02.046
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Air sparging is recognized as an effective way to increase permeate flux in membrane filtration processes. The application of air sparging with an external-loop airlift ceramic membrane bioreactor was studied at different gas flow rates, biomass concentrations and suction pressures. A 180% increase in permeate flux was obtained while filtering a 2g/L activated sludge wastewater suspension with the airlift cross-flow operation for U-g = 0.21 m/s. The mechanism of flux enhancement in the case of slug flow in tubular membrane was discussed. The region near the gas slug was divided into three different zones: falling film zone, wake zone and remaining liquid slug zone. Air sparging significantly lowered cake thickness and consequently cake resistances for the wake region and the failing film region. A novel model combining hydrodynamic of gas-liquid two-phase flow and cake resistance was developed to simulate the process. The model was validated with experimental data with an error of 8.3%. (C) 2009 Elsevier Ltd. All rights reserved.
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页码:2859 / 2865
页数:7
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