2013
DOI: 10.1016/j.seppur.2013.03.030
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Hydrophilic composite membranes for simultaneous separation and photocatalytic degradation of organic pollutants

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Cited by 77 publications
(35 citation statements)
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“…The flux decline was~89.6% lower on the TiO 2 /Al 2 O 3 composite membrane than on the bare Al 2 O 3 membrane (1.25 vs. 0.13 LMH h −1 ). The higher fouling rate in the bare Al 2 O 3 membrane results from the higher probability of pore fouling in the larger pores of the bare membrane than in the smaller pores of the TiO 2 /Al 2 O 3 composite membrane [23]. The previous results also confirmed that the membrane permeability decreased significantly after immobilizing a TiO 2 layer on the Al 2 O 3 membrane support, as shown in Table 1.…”
Section: Membrane Morphologysupporting
confidence: 62%
See 1 more Smart Citation
“…The flux decline was~89.6% lower on the TiO 2 /Al 2 O 3 composite membrane than on the bare Al 2 O 3 membrane (1.25 vs. 0.13 LMH h −1 ). The higher fouling rate in the bare Al 2 O 3 membrane results from the higher probability of pore fouling in the larger pores of the bare membrane than in the smaller pores of the TiO 2 /Al 2 O 3 composite membrane [23]. The previous results also confirmed that the membrane permeability decreased significantly after immobilizing a TiO 2 layer on the Al 2 O 3 membrane support, as shown in Table 1.…”
Section: Membrane Morphologysupporting
confidence: 62%
“…Such a membrane permeability enhancement can be resulted from improvement of the membrane wettability or higher water temperature induced by the UV irradiation [15,22]. The TiO 2 coating layer can improve surface hydrophilicity under UV radiation due to the production of the hydroxyl groups on membrane [23]. In addition, temperature increase can reduce water viscosity, thereby increasing membrane permeability [22].…”
Section: Membrane Morphologymentioning
confidence: 99%
“…TiO 2 particles and polar organic functional groups could be immobilized together onto membrane surface, and thereby the immobilization of catalyst and membrane surface modification occurs simultaneously. Based on above, hydrophilicity and antifouling ability of membrane surface can be enhanced due to minimization of mass transfer resistance between the semi-conductor surface and fluid bulk via the forced transport of reactants by convection [5]. Great variety of materials has been used for the membrane surface modification, such as TiO 2 nanotubes [6], TiO 2 -graphene oxide (GO) [7][8][9], carbon nanotubes (CNTs) [10][11][12][13], etc.…”
Section: Introductionmentioning
confidence: 99%
“…However, the use of filtration system wastes both time and money. In recent years, photocatalyst film reactors have attracted significant attention because these systems integrate the advantages of film separation (high separation efficiency, easy operation, low energy consumption, and no secondary pollution) and photocatalysis technique [26][27][28][29][30]. However, Ag@AgX film reactors were less studied compared to the powdery Ag@AgX photocatalysts [31][32][33].…”
Section: Introductionmentioning
confidence: 99%