2014
DOI: 10.1016/j.memsci.2014.05.030
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A systematic analysis of fouling evolution and irreversibility behaviors of MBR supernatant hydrophilic/hydrophobic fractions during microfiltration

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Cited by 51 publications
(26 citation statements)
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“…This is also in accordance to the work of Yin et al [125]: they confirmed that as the TMP varied to 300 psi, the permeate flux increased from 39 to 59 L/m 2 h. However, the major defects attributed to these operating conditions were the excessive energy demand (12 kW/m 3 ) for aeration and the lofty fouling susceptibility [121]. Equally, studies conducted by Le-Clech et al [108], Morrow et al [113], Xiao et al [126], and Abdurahman et al [127] reported comparable results, as presented in Table 2. Notes: EDP = energy demand for permeate, EDA = energy demand for aeration, NA = not available.…”
Section: Effect Of Mbr Configurationsupporting
confidence: 82%
“…This is also in accordance to the work of Yin et al [125]: they confirmed that as the TMP varied to 300 psi, the permeate flux increased from 39 to 59 L/m 2 h. However, the major defects attributed to these operating conditions were the excessive energy demand (12 kW/m 3 ) for aeration and the lofty fouling susceptibility [121]. Equally, studies conducted by Le-Clech et al [108], Morrow et al [113], Xiao et al [126], and Abdurahman et al [127] reported comparable results, as presented in Table 2. Notes: EDP = energy demand for permeate, EDA = energy demand for aeration, NA = not available.…”
Section: Effect Of Mbr Configurationsupporting
confidence: 82%
“…Besides, at relatively low pH of the wastewater and recovery solution (Supporting Information, Fig. S1 ), the primary species of humic acid and bicarbonate are in molecular forms with neutral charge 40 , thus their migration competing with nutrient ions might be relatively weak. Further research on real wastewater is needed to investigate the dynamic balance between concentrated NH 4 + and PO 4 3− and other types of ions in the recovery solution during the long-term operation.…”
Section: Discussionmentioning
confidence: 99%
“…Characteristic fouling stages and the transition points between them can be quantitatively evaluated by a detailed investigation of the obtained resistance vs. permeate volume (R vs. V) curves, combined with the classical filtration laws [27] described by the dR/dV vs. R relationship [28,29] as…”
Section: Theorymentioning
confidence: 99%
“…to describe fouling evolution and gel layer growth during constant pressure stirred dead-end filtration [28,29]. Fig.…”
Section: Theorymentioning
confidence: 99%