The effects of the pore geometry on yeast cell fouling during microfiltration were studied using novel micro-patterned membranes having well-defined slot-shaped or circular pores. Normal flow filtration experiments were performed with Baker's yeast suspensions. The flux decline data were consistent
Pore fouling of microfiltration membranes by activated sludge
β Scribed by Herbert H.P. Fang; Xinlong Shi
- Publisher
- Elsevier Science
- Year
- 2005
- Tongue
- English
- Weight
- 319 KB
- Volume
- 264
- Category
- Article
- ISSN
- 0376-7388
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β¦ Synopsis
Pore fouling of four microfiltration membranes was investigated for the filtration of activated sludge using sonication as the means to remove the cake layer from membrane surface. Results show that pore fouling was affected by membrane's microstructure, pore openings and hydrophilicity. For the track-etched polycarbonate (PC) membrane, there was no measurable pore resistance (R p ) to filtration. For the three membranes of sponge-like microstructure, the respective R p values were 0.3 Γ 10 11 , 1.3 Γ 10 11 , and 16.4 Γ 10 11 m -1 for polyvinylidene fluoride (PVDF), mixed cellulose esters (MCE), and polyethersulfone (PES). The PES membrane had the highest R p due to its large pore openings (18-20 m), whereas MCE had higher R p than PVDF because of its higher hydrophilicity. The R p of PES membrane accounted for 86% of the total resistance for its filtration of activated sludge; the corresponding values were merely 2% for PVDF and 11% for MCE. It increased with the suspended solids level of the activated sludge to the power of 0.56. Results further demonstrated that R p -dominant type of membranes, such as PES, was unsuitable for the membrane bioreactors.
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