2012
DOI: 10.1080/19443994.2012.696820
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Surface modification of polyethersulfone ultrafiltration (PES-UF) membrane using myoglobin as modifying agent

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Cited by 9 publications
(5 citation statements)
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“…An increasing pattern of permeate water flux was observed with increase in the concentration of the Fe 2 O 3 nanoparticle upto 0.5 wt%. This can be explained by the presence of finger like support layer in the membrane as revealed by the SEM micro graphs [11,37]. However, the water flux decreased for PES/CA blend membranes with more than 0.5 wt% Fe 2 O 3 nanoparticles.…”
Section: Water Uptakementioning
confidence: 97%
See 1 more Smart Citation
“…An increasing pattern of permeate water flux was observed with increase in the concentration of the Fe 2 O 3 nanoparticle upto 0.5 wt%. This can be explained by the presence of finger like support layer in the membrane as revealed by the SEM micro graphs [11,37]. However, the water flux decreased for PES/CA blend membranes with more than 0.5 wt% Fe 2 O 3 nanoparticles.…”
Section: Water Uptakementioning
confidence: 97%
“…Polyethersulfone (PES) is widely used in the synthesis of ultra filtration membrane for treating water and wastewater [6,7]. Polyethersulfone is a highly stable polymer in terms of material characteristics [8,9] exhibiting splendid film forming and mechanical properties combined with excellent thermal, oxidative and hydrolytic strength [10,11]. Cellulose acetate (CA) membranes have good toughness and better fouling resistance as compared to PES and an appreciable desalting behavior [6].…”
Section: Introductionmentioning
confidence: 99%
“…Specifically, researchers have modified the surface of the membrane, or they have integrated molecules into the body of the membrane. Membranes coated with hydrophilic polymers, reactive nanomaterials, or nanotopographic features offer a number of advantages over their mixed-matrix counterparts, such as concentrating the active material at the surface of the membrane and tailoring an already optimized ultrafiltration membrane. Unfortunately, surface modifications that effectively advance one property, for example, increasing the flux of the membrane, often impede a different property, such as selectivity. Therefore, a different approach that alters ultrafiltration membranes without adversely impacting their flux or selectivity is needed.…”
Section: Introductionmentioning
confidence: 99%
“…Prior to use, all membranes were flushed using a custom-built cross-flow cell (28 mm long, 17 mm wide, and 1.5 mm deep, with an active area of 5.44 cm 2 ) equipped with a 31 mil (0.7874 mm) low foulant spacer and a permeate carrier (Sterlitech Corporation, Kent, WA), consistent with our previous study . All tests were conducted at a flow rate of 50 mL/min enabled by a reciprocating pump (Eldex Laboratories Incorporated, Napa, CA) followed by a dampener (Cat Pumps, Minneapolis, MN). Two distinct flushing procedures were used on the two commercial membranes following industry recommendations. To flush the Millipore membranes (29 mm × 45 mm), they were placed active side down in the cross-flow cell and flushed with DI water at a transmembrane pressure (TMP) of 1.5 bar (21.8 psi), where the TMP was held for 0.016 h to remove glycerol (a preservation substance) as confirmed by high-performance liquid chromatography (HPLC).…”
Section: Methodsmentioning
confidence: 99%