Effects of operative conditions on membrane fouling of jet loop membrane bioreactor
The orthogonal experiments, which involves three factors: aeration intensity, suction time and suction suspended time, were designed to research membrane fouling of jet loop membrane bioreactor (JLMBR). Experimental results indicate that increasing aeration intensity, reducing suction time and incre...
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Published in | Journal of Shanghai University Vol. 14; no. 4; pp. 251 - 254 |
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Main Author | |
Format | Journal Article |
Language | English |
Published |
Heidelberg
Shanghai University Press
01.08.2010
School of Environmental and Chemical Engineering, Shanghai University, Shanghai 200444, P. R. China Shanghai Environmental Protection Bureau, Shanghai 200003, P. R. China%School of Environmental and Chemical Engineering, Shanghai University, Shanghai 200444, P. R. China |
Subjects | |
Online Access | Get full text |
ISSN | 1007-6417 1863-236X |
DOI | 10.1007/s11741-010-0639-2 |
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Abstract | The orthogonal experiments, which involves three factors: aeration intensity, suction time and suction suspended time, were designed to research membrane fouling of jet loop membrane bioreactor (JLMBR). Experimental results indicate that increasing aeration intensity, reducing suction time and increasing suction suspended time all could mitigate membrane fouling effectively. However excessive aeration intensity, too short suction time and excessive suction suspended time were bad for bioreactor running. The optimal aeration intensity, suction time and suction suspended time were 0.75 1.00 m3/(m2.h), 8 -10 min and 4 -5 min, respectively. The three factors all had effect on membrane pollution rate, while the suction time was the most important one and followed by aeration intensity and suction suspended time. It also indicates that, comparing with traditional submerged membrane bioreactors, JLMBR had lower membrane pollution rate. |
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AbstractList | The orthogonal experiments, which involves three factors: aeration intensity, suction time and suction suspended time, were designed to research membrane fouling of jet loop membrane bioreactor (JLMBR). Experimental results indicate that increasing aeration intensity, reducing suction time and increasing suction suspended time all could mitigate membrane fouling effectively. However excessive aeration intensity, too short suction time and excessive suction suspended time were bad for bioreactor running. The optimal aeration intensity, suction time and suction suspended time were 0.75–1.00 m
3
/(m
2
·h), 8–10 min and 4–5 min, respectively. The three factors all had effect on membrane pollution rate, while the suction time was the most important one and followed by aeration intensity and suction suspended time. It also indicates that, comparing with traditional submerged membrane bioreactors, JLMBR had lower membrane pollution rate. The orthogonal experiments, which involves three factors: aeration intensity, suction time and suction suspended time, were designed to research membrane fouling of jet loop membrane bioreactor (JLMBR). Experimental results indicate that increasing aeration intensity, reducing suction time and increasing suction suspended time all could mitigate membrane fouling effectively. However excessive aeration intensity, too short suction time and excessive suction suspended time were bad for bioreactor running. The optimal aeration intensity, suction time and suction suspended time were 0.75 1.00 m3/(m2.h), 8 -10 min and 4 -5 min, respectively. The three factors all had effect on membrane pollution rate, while the suction time was the most important one and followed by aeration intensity and suction suspended time. It also indicates that, comparing with traditional submerged membrane bioreactors, JLMBR had lower membrane pollution rate. O6; The orthogonal experiments, which involves three factors: aeration intensity, suction time and suction suspended time, were designed to research membrane fouling of jet loop membrane bioreactor (JLMBR). Experimental results indicate that increasing aeration intensity, reducing suction time and increasing suction suspended time all could mitigate membrane fouling effectively. However excessive aeration intensity, too short suction time and excessive suction suspended time were bad for bioreactor running. The optimal aeration intensity, suction time and suction suspended time were 0.75-1.00 m3/(m2.h),8-10 min and 4-5 min, respectively. The three factors all had effect on membrane pollution rate, while the suction time was the most important one and followed by aeration intensity and suction suspended time. It also indicates that, comparing with traditional submerged membrane bioreactors, JLMBR had lower membrane pollution rate. |
Author | 徐高田 孙佳琳 秦哲 阮慧娟 |
AuthorAffiliation | School of Environmental and Chemical Engineering, Shanghai University, Shanghai 200444, P. R. China Shanghai Environmental Protection Bureau, Shanghai 200003, P. R. China |
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Cites_doi | 10.1016/j.desal.2004.07.035 10.1016/S0376-7388(01)00525-7 10.1016/0009-2509(93)80124-9 10.1016/j.procbio.2003.11.028 |
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Keywords | membrane fouling suction time suction suspended time jet loop membrane bioreactor (JLMBR) aeration intensity |
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References_xml | – reference: ParkJ. S.YeonK. M.LeeC. H.Hydrodynamics and microbial physiology affecting performance of a new MBR, membrane-coupled high-performance compact reactor [J]Desalination2005172218118810.1016/j.desal.2004.07.035 – reference: FarizogluB.KeskinlerB.YildizE.NuhogluA.Cheese whey treatment performance of an aerobic jet loop membrane bioreactor [J]Process Biochemistry200439122283229110.1016/j.procbio.2003.11.028 – reference: GuiP.HuangX.ChenY.WenX. H.QianY.Influence of the operation parameters on membrane filtration [J]Chinese Journal of Environmental Science19992033841 – reference: LivingstonA. G.ZhangS. F.Hydrodynamic behaviour of three-phase (gas-liquid-solid) airlift reactors [J]Chemical Engineering Science19934891641165410.1016/0009-2509(93)80124-9 – reference: VieiraM.Application of ultrafiltration complexation process for metal removal from pulp and paper industry wastewater [J]Journal of Membrane Science2001194227327610.1016/S0376-7388(01)00525-7 – reference: Jet loop membrane bioreactor device: China, ZL 2007 20068420.9 [P]. 2008-02-13. – reference: WeiC.-h.XieB.ZhangX.-z.QianYu.Relationship between reactor performances and structural parameters of inner-loop three-phase fluidized bed [J]Journal of Chemical Engineering of Chinese University2001153236241 – volume: 172 start-page: 181 issue: 2 year: 2005 ident: 639_CR2 publication-title: Desalination doi: 10.1016/j.desal.2004.07.035 – ident: 639_CR1 – volume: 194 start-page: 273 issue: 2 year: 2001 ident: 639_CR4 publication-title: Journal of Membrane Science doi: 10.1016/S0376-7388(01)00525-7 – volume: 48 start-page: 1641 issue: 9 year: 1993 ident: 639_CR6 publication-title: Chemical Engineering Science doi: 10.1016/0009-2509(93)80124-9 – volume: 15 start-page: 236 issue: 3 year: 2001 ident: 639_CR7 publication-title: Journal of Chemical Engineering of Chinese University – volume: 20 start-page: 38 issue: 3 year: 1999 ident: 639_CR5 publication-title: Chinese Journal of Environmental Science – volume: 39 start-page: 2283 issue: 12 year: 2004 ident: 639_CR3 publication-title: Process Biochemistry doi: 10.1016/j.procbio.2003.11.028 |
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Snippet | The orthogonal experiments, which involves three factors: aeration intensity, suction time and suction suspended time, were designed to research membrane... The orthogonal experiments, which involves three factors: aeration intensity, suction time and suction suspended time, were designed to research membrane... O6; The orthogonal experiments, which involves three factors: aeration intensity, suction time and suction suspended time, were designed to research membrane... |
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SubjectTerms | Classical Mechanics Engineering Environment Environmental and Chemical Engineering Life Sciences Materials Science Mathematical and Computational Engineering MBR膜 Mechatronics 一体式膜生物反应器 喷射环流 手术 暂停时间 曝气强度 正交实验 膜污染 |
Title | Effects of operative conditions on membrane fouling of jet loop membrane bioreactor |
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