2018
DOI: 10.1016/j.memsci.2018.08.067
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Understanding membrane fouling by oil-in-water emulsion via experiments and molecular dynamics simulations

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Cited by 67 publications
(60 citation statements)
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“…The COD is lower for Samples N1 and N3 and differs by 8%, while the COD difference between N2 and N3 exceeded 23%. Higher organic pollutant content in Sample N2 caused an increase in cake layer formation (Tanis-Kanbur et al, 2018) and consequently lower emulsion flux. The limiting flux of 100 L/(m 2 •h) was reached with acidic samples N1 and N3, as shown in Fig.…”
Section: Uf Operationmentioning
confidence: 95%
See 1 more Smart Citation
“…The COD is lower for Samples N1 and N3 and differs by 8%, while the COD difference between N2 and N3 exceeded 23%. Higher organic pollutant content in Sample N2 caused an increase in cake layer formation (Tanis-Kanbur et al, 2018) and consequently lower emulsion flux. The limiting flux of 100 L/(m 2 •h) was reached with acidic samples N1 and N3, as shown in Fig.…”
Section: Uf Operationmentioning
confidence: 95%
“…8. Most likely, negatively charged surfactants are attached to the membrane surface and influence its surface charge (Tanis-Kanbur et al, 2018). As the conductivity is very high, it is assumed that many charged ions are present in waste emulsion, and contribute to the membrane surface charge.…”
Section: Zeta Potential Of Fouled Membranementioning
confidence: 99%
“…Modeling of membrane fouling behavior was studied in several publications. Tanis‐Kanbur, Velioglu, Tanudjaja, Hu, and Chew (2018) modeled fouling from oily wastewater to evaluate flux and found that the mechanisms were different at various droplet studies and the use of surfactants.…”
Section: Modelingmentioning
confidence: 99%
“…The shape and charge of the surfactant head can significantly affect the fouling tendency. The latest study by Tanis-Kanbur et al evidenced that the highest critical flux was obtained in the absence of surfactant stabilization due to the stronger oil-water interaction over oil-membrane interaction, hence the oil droplets remain in the bulk aqueous feed [63]. When the oil emulsion was stabilized with cationic surfactant dodecyltrimethylammonium bromide (DTAB), the lowest critical flux was achieved as the weak oil–oil repulsion has resulted in the extensive coalescence of the oil droplets.…”
Section: Membrane Technology For Oily Wastewater Treatmentmentioning
confidence: 99%