Comparison of Polytetrafluoroethylene Flat-Sheet Membranes with Different Pore Sizes in Application to Submerged Membrane Bioreactor
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Nittami, Tadashi
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Hitomi, Tetsuo
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Yokohama Natl Univ, Dept Chem Engn, Hodogaya Ku, 79-5 Tokiwadai, Yokohama, Kanagawa 2408501, JapanYokohama Natl Univ, Dept Chem Engn, Hodogaya Ku, 79-5 Tokiwadai, Yokohama, Kanagawa 2408501, Japan
Hitomi, Tetsuo
[1
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Matsumoto, Kanji
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Yokohama Natl Univ, Dept Chem Engn, Hodogaya Ku, 79-5 Tokiwadai, Yokohama, Kanagawa 2408501, JapanYokohama Natl Univ, Dept Chem Engn, Hodogaya Ku, 79-5 Tokiwadai, Yokohama, Kanagawa 2408501, Japan
Matsumoto, Kanji
[1
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Nakamura, Kazuho
[1
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Ikeda, Takaharu
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Nippon Valqua Ind Ltd, Corp Res Div, Machida, Tokyo 1940215, JapanYokohama Natl Univ, Dept Chem Engn, Hodogaya Ku, 79-5 Tokiwadai, Yokohama, Kanagawa 2408501, Japan
Ikeda, Takaharu
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Setoguchi, Yoshihiro
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Nippon Valqua Ind Ltd, Corp Res Div, Machida, Tokyo 1940215, JapanYokohama Natl Univ, Dept Chem Engn, Hodogaya Ku, 79-5 Tokiwadai, Yokohama, Kanagawa 2408501, Japan
Setoguchi, Yoshihiro
[2
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Motoori, Manabu
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Nippon Valqua Ind Ltd, Corp Res Div, Machida, Tokyo 1940215, JapanYokohama Natl Univ, Dept Chem Engn, Hodogaya Ku, 79-5 Tokiwadai, Yokohama, Kanagawa 2408501, Japan
Motoori, Manabu
[2
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[1] Yokohama Natl Univ, Dept Chem Engn, Hodogaya Ku, 79-5 Tokiwadai, Yokohama, Kanagawa 2408501, Japan
[2] Nippon Valqua Ind Ltd, Corp Res Div, Machida, Tokyo 1940215, Japan
This study focused on phase separation of activated sludge mixed liquor by flat-sheet membranes of polytetrafluoroethylene (PTFE). A 20 liter working volume lab-scale MBR incorporating immersed PTFE flat-sheet membrane modules with different pore sizes (0.3, 0.5 and 1.0 mu m) was operated for 19 days treating a synthetic wastewater. The experiment was interrupted twice at days 5 and 13 when the modules were removed and cleaned physically and chemically in sequence. The pure water permeate flux of each membrane module was measured before and after each cleaning step to calculate membrane resistances. Results showed that fouling of membrane modules with 0.3 mu m pore size was more rapid than other membrane modules with different pore sizes (0.5 and 1.0 mu m). On the other hand, it was not clear whether fouling of the 0.5 mu m membrane module was more severe than that of the 1.0 mu m membrane module. This was partly because of the membrane condition after chemical cleaning, which seemed to determine the fouling of those modules over the next period. When irreversible resistance (Ri) i.e., differences in membrane resistance before use and after chemical cleaning was high, the transmembrane pressure increased quickly during the next period irrespective of membrane pore size.
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Univ New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, AustraliaUniv New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, Australia
Le-Clech, Pierre
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Chen, Vicki
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Univ New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, AustraliaUniv New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, Australia
Chen, Vicki
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Fane, Tony A. G.
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Univ New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, AustraliaUniv New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, Australia
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Univ New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, AustraliaUniv New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, Australia
Le-Clech, Pierre
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Chen, Vicki
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Univ New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, AustraliaUniv New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, Australia
Chen, Vicki
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Fane, Tony A. G.
论文数: 0引用数: 0
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Univ New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, AustraliaUniv New S Wales, Sch Chem Engn, UNESCO Ctr Membrane Sci & Technol, Sydney, NSW 2052, Australia