2008
DOI: 10.1016/j.desal.2007.12.010
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Prediction of the circulation velocity in a membrane bioreactor

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Cited by 42 publications
(32 citation statements)
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“…Both these aspects were taken into account by modifying the Chisti model accordingly [166,169]. In contrast to the slender airlift reactors studied by Chisti et al, MBR tanks typically have significantly different width/height and riser/downcomer cross-section area ratios.…”
Section: Two-phase Flowmentioning
confidence: 99%
“…Both these aspects were taken into account by modifying the Chisti model accordingly [166,169]. In contrast to the slender airlift reactors studied by Chisti et al, MBR tanks typically have significantly different width/height and riser/downcomer cross-section area ratios.…”
Section: Two-phase Flowmentioning
confidence: 99%
“…the turbulence is generated by aeration. However, turbulence promotion by aeration needs large bubbles [7], leading to a low oxygen transfer efficiency. Intense aeration may also damage flocs structure through releasing extracel-*Corresponding author.…”
Section: Introductionmentioning
confidence: 99%
“…In order to control fouling with a minimal energy cost, it should be of great significance to optimize the hydraulic condition in the aerated membrane tanks. Baffles play a vital role in the commonly applied airlift MBRs (Liu et al, 2003;Prieske et al, 2008). They divide the membrane tank into a downcomer and an aerated riser section where membranes are usually located.…”
Section: Introductionmentioning
confidence: 99%
“…However, membrane fouling remains as a challenge for the practical application of MBRs. An important issue associated with membrane fouling is the high energy consumption involved in aeration in membrane tank for fouling control (Liu et al, 2000;Prieske et al, 2008). The power used for aeration in membrane tank could take up about 30-50% of the overall energy consumption for MBR operation.…”
Section: Introductionmentioning
confidence: 99%