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
中国国家自然科学基金; 中国博士后科学基金;
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.
引用
收藏
页码:2859 / 2865
页数:7
相关论文
共 26 条
  • [1] Gas sparging to enhance permeate flux in ultrafiltration using hollow fibre membranes
    Bellara, SR
    Cui, ZF
    Pepper, DS
    [J]. JOURNAL OF MEMBRANE SCIENCE, 1996, 121 (02) : 175 - 184
  • [2] Brindle K, 1996, BIOTECHNOL BIOENG, V49, P601, DOI 10.1002/(SICI)1097-0290(19960320)49:6<601::AID-BIT1>3.0.CO
  • [3] 2-S
  • [4] How slug flow can improve ultrafiltration flux in organic hollow fibres
    Cabassud, C
    Laborie, S
    Laine, JM
    [J]. JOURNAL OF MEMBRANE SCIENCE, 1997, 128 (01) : 93 - 101
  • [5] Investigation of biological and fouling characteristics of submerged membrane bioreactor process for wastewater treatment by model sensitivity analysis
    Cho, JW
    Ahn, KH
    Lee, YH
    Lim, BR
    Kim, JY
    [J]. WATER SCIENCE AND TECHNOLOGY, 2004, 49 (02) : 245 - 254
  • [6] The use of gas bubbling to enhance membrane processes
    Cui, ZF
    Chang, S
    Fane, AG
    [J]. JOURNAL OF MEMBRANE SCIENCE, 2003, 221 (1-2) : 1 - 35
  • [7] Treatment and reuse of toilet wastewater by an airlift external circulation membrane bioreactor
    Fan, Yaobo
    Li, Gang
    Wu, Linlin
    Yang, Wenbo
    Dong, Chunsong
    Xu, Huifang
    Fan, Wei
    [J]. PROCESS BIOCHEMISTRY, 2006, 41 (06) : 1364 - 1370
  • [8] Fane A.G., 1991, FILTR SEPARAT, P332, DOI DOI 10.1016/0015-1882(91)80157-Z
  • [9] Aerobic MBRs for domestic wastewater treatment: a review with cost considerations
    Gander, M
    Jefferson, B
    Judd, S
    [J]. SEPARATION AND PURIFICATION TECHNOLOGY, 2000, 18 (02) : 119 - 130
  • [10] Mass transfer in gas-sparged ultrafiltration: upward slug flow in tubular membranes
    Ghosh, R
    Cui, ZF
    [J]. JOURNAL OF MEMBRANE SCIENCE, 1999, 162 (1-2) : 91 - 102