2021
DOI: 10.1007/s10965-021-02644-5
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The effect of unique structural flower-like TiO2 towards polysulfone mixed matrix membrane as efficient antifouling and antibacterial for humic acid removal

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Cited by 5 publications
(5 citation statements)
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“…The air resistance in the composite process is derived from the resistance of the membrane and the substrate (determined by its own structural parameters), the layer–layer resistance generated after stacking, the resistance of the gridded fiber, and the resistance generated during the membrane pore blocking (determined by the composite parameters). According to Darcy’s law, the calculation model of the resistance in the composite process is established as shown in eqs –. R normalt = R normalm + R normals + R normala + R normalb + R normalc R normali = normalΔ P normali J normali · μ R normalt = normalΔ P normalm J normalm · μ + normalΔ P normals J normals · μ + normalΔ P normala J normala · μ + normalΔ P normalb J normalb · μ + normalΔ P normalc …”
Section: Methodsmentioning
confidence: 99%
See 2 more Smart Citations
“…The air resistance in the composite process is derived from the resistance of the membrane and the substrate (determined by its own structural parameters), the layer–layer resistance generated after stacking, the resistance of the gridded fiber, and the resistance generated during the membrane pore blocking (determined by the composite parameters). According to Darcy’s law, the calculation model of the resistance in the composite process is established as shown in eqs –. R normalt = R normalm + R normals + R normala + R normalb + R normalc R normali = normalΔ P normali J normali · μ R normalt = normalΔ P normalm J normalm · μ + normalΔ P normals J normals · μ + normalΔ P normala J normala · μ + normalΔ P normalb J normalb · μ + normalΔ P normalc …”
Section: Methodsmentioning
confidence: 99%
“…The air resistance in the composite process is derived from the resistance of the membrane and the substrate (determined by its own structural parameters), the layer–layer resistance generated after stacking, the resistance of the gridded fiber, and the resistance generated during the membrane pore blocking (determined by the composite parameters). According to Darcy’s law, the calculation model of the resistance in the composite process is established as shown in eqs –. In the above equations, R t refers to the air resistance, 1/ m ; R m refers to the ePTFE resistance, 1/ m ; R s refers to the PPS resistance, 1/ m ; R a refers to the interface resistance after stacking, 1/ m ; R b refers to the GF resistance, 1/ m ; R c refers to the resistance caused by pore blockage, 1/ m ; Δ P i refers to the pressure drop, Pa; μ refers to the gas viscosity, Pa·s; J i refers to the permeation flux, m 3 /(m 2 ·h·kPa).…”
Section: Methodsmentioning
confidence: 99%
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“…A pressure-driven process is commonly used to separate dye wastewater. There are four classes of pressure-driven processes, which are microfiltration (MF), ultrafiltration (UF), nanofiltration (NF), and reverse osmosis (RO) [72], [73]. MF possess larger pore size around 0.1 to 10 µm thus the membrane is not suitable to be used for dye wastewater treatment.…”
Section: Membrane Filtration Techniquementioning
confidence: 99%
“…In the past, membranes were pretreated with chlorine for efficient disinfection; however, chlorine and their derivatives often cause membrane degradation and produce harmful byproducts ( Yu et al., 2014 ). Recently, many reports have demonstrated that incorporation of metal/metal oxide/metal sulfide, carbon-based nanomaterial into the membrane is an effective strategy to circumvent the issues related to biofouling of membrane, thereby restoring the enhanced the separation performance in terms of rejection and stability ( Azhar et al., 2021 ; Liu et al., 2017 ; Nain et al., 2020b ; Rajakumaran et al., 2020 ; Zhao et al., 2021 ).…”
Section: Wastewater Treatmentmentioning
confidence: 99%