2011
DOI: 10.1007/s13201-011-0021-2
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Development of polyaniline-modified polysulfone nanocomposite membrane

Abstract: In the present investigation, polyaniline (PANI) nanoparticles were used to improve the separation figures of merit of polysulfone (PSu) membrane. Polyaniline nanoparticles were dispersed into polysulfone matrix for the development of PSu/PANI nanocomposites through solution blending. A wet phase inversion method was used to fabricate a flat sheet polysulfone (PSu) and PSu/PANI nanocomposite membranes. The structure and characteristic properties of the membranes were investigated in terms of the surface and cr… Show more

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Cited by 47 publications
(31 citation statements)
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“…Pure water flux of synthesized membranes was calculated on a dead‐end filtration setup (HP4750 Stirred Cell, Sterlitech, USA), with a provision to hold a 4.7 cm diameter membrane. At room temperature, the membranes were compressed for 1 h at constant pressure and then the pure water flux was calculated using Equation : J=V/true(normalA*normalttrue) where J is pure water flux (L/m 2 h), V is volume of permeated water (L), A is effective membrane area (m 2 ), and t is time (h) necessary to collect permeated water of volume, V. The water permeability was calculated using Equation : normalLnormalp=J/ΔP where L p is water permeability (L/m 2 hkPa), J is pure water flux (L/m 2 h), and ΔP is operational pressure (kPa). The percentage porosity, % ϵ, was determined by measuring the weight loss of the membrane and calculated using Equation …”
Section: Methodsmentioning
confidence: 99%
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“…Pure water flux of synthesized membranes was calculated on a dead‐end filtration setup (HP4750 Stirred Cell, Sterlitech, USA), with a provision to hold a 4.7 cm diameter membrane. At room temperature, the membranes were compressed for 1 h at constant pressure and then the pure water flux was calculated using Equation : J=V/true(normalA*normalttrue) where J is pure water flux (L/m 2 h), V is volume of permeated water (L), A is effective membrane area (m 2 ), and t is time (h) necessary to collect permeated water of volume, V. The water permeability was calculated using Equation : normalLnormalp=J/ΔP where L p is water permeability (L/m 2 hkPa), J is pure water flux (L/m 2 h), and ΔP is operational pressure (kPa). The percentage porosity, % ϵ, was determined by measuring the weight loss of the membrane and calculated using Equation …”
Section: Methodsmentioning
confidence: 99%
“…Electrically conductive polymers are used as a part of the thin‐film composite membrane. They can be easily deposited as the coating medium on a wide variety of supporting materials, such as porous metals, filter paper, ion‐exchange membranes, microfiltration membranes, fibres, stainless steel, and polymer membranes . There are several methods reported for the membrane synthesis.…”
Section: Introductionmentioning
confidence: 99%
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“…C f and C p are the polyethylene glycol concentrations in the feed solution and permeate solution, respectively [37]. The concentration of PEG was determined based on their absorbency in a UV-spectrophotometer at a wavelength of 535 nm.…”
Section: Membranes Characterizationmentioning
confidence: 99%
“…Extensive research works have been carried out to develop NF/UF membranes that can be used to fulfill the above separations [4][5][6][7][8][9][10][11][12]. Although commercial polymeric membranes are readily available in the market such as cellulose acetates, polyethersulfones, polysulfones, and polyacrylonitrile, but these membranes usually have fixed physico-chemical properties which limit any separation to the fixed selectivity of their constituents [13][14][15].…”
Section: Introductionmentioning
confidence: 99%