2010
DOI: 10.1016/j.memsci.2009.09.040
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A systematic insight into fouling propensity of soluble microbial products in membrane bioreactors based on hydrophobic interaction and size exclusion

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Cited by 134 publications
(50 citation statements)
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“…For the initial stage of fouling, it was found that HIS was the most responsible for the rapid flux decline in the initial stage of microfiltration using hydrophilically enhanced PVDF membrane, and that the role of the fraction of HIS with MW > 100 kDa was particularly prominent despite its relatively low abundance [82]. This should be ascribed to steric effect rather than hydrophobic affinity between membrane and foulant.…”
Section: Fouling Mechanismsmentioning
confidence: 99%
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“…For the initial stage of fouling, it was found that HIS was the most responsible for the rapid flux decline in the initial stage of microfiltration using hydrophilically enhanced PVDF membrane, and that the role of the fraction of HIS with MW > 100 kDa was particularly prominent despite its relatively low abundance [82]. This should be ascribed to steric effect rather than hydrophobic affinity between membrane and foulant.…”
Section: Fouling Mechanismsmentioning
confidence: 99%
“…Both of the properties could be qualitatively determined via column chromatography method based on differential adsorption and elution [81][82], yielding hydrophilic/hydrophobic fractions and acid/base/ neutral fractions. Another useful method for determining hydrophobicity is the bacterial adherence to hydrocarbons (BATH) test based on the partition of the target (bacteria) between aqueous phase and hydrocarbon droplet surface [83]; this method has recently been applied to the case of sludge flocs with the result termed relative hydrophobicity (RH) [84].…”
Section: Membrane Foulingmentioning
confidence: 99%
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“…The flux decline of UF in the dead-end cell under constant pressure could be described by different blocking mechanisms: complete blocking, standard blocking, intermediate blocking and cake filtration (Shen et al, 2010). The equations for different membrane blocking mechanisms are listed below: (1) Complete blocking: ÀJ + J 0 = aV; (2) Standard blocking: 1/t + b = J 0 /V; (3) Intermediate blocking: Àln J + lnJ 0 = cV; (4) Cake filtration: 1/JÀ1/J 0 = dV, where V is the volume of the feed water; a, b, c and d are all constants.…”
Section: Modeling For Membrane Fouling Processmentioning
confidence: 99%