1987
DOI: 10.1016/0011-9164(87)87013-3
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A review of fouling and fouling control in ultrafiltration

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Cited by 302 publications
(151 citation statements)
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“…Membrane fouling, the process by which foulants, namely colloidal (e.g., clays, flocs), biological (e.g., bacteria, fungi), organic (e.g., oils, polyelectrolytes, humic substances), and scaling (e.g., mineral precipitates in RO systems) foulants, deposit onto the membrane surface or in the membrane pores [72,73], may take different forms, the main mechanisms of which are adsorption (physical and/or chemical), pore blocking, deposition of a cake layer, and gel formation [74][75][76][77][78][79]. The extent of fouling, which stems from the nature of foulant-membrane interaction, is a complex function of the feed characteristics (e.g., foulant type, foulant concentration, and physicochemical properties of the foulants such as the functional groups, charge, size, and conformation [72,[80][81][82]), operating conditions (e.g., inadequate pretreatment, inadequate control of the hydrodynamics of the system, excessive flux, and low cross-flow velocity (in cross-flow systems) [72,[82][83][84]), and membrane properties (e.g., pore-size distribution, surface roughness, charge properties, and hydrophobicity [70,[85][86][87]). …”
Section: Fouling and Concentration Polarization In Submerged Hf Systemsmentioning
confidence: 99%
“…Membrane fouling, the process by which foulants, namely colloidal (e.g., clays, flocs), biological (e.g., bacteria, fungi), organic (e.g., oils, polyelectrolytes, humic substances), and scaling (e.g., mineral precipitates in RO systems) foulants, deposit onto the membrane surface or in the membrane pores [72,73], may take different forms, the main mechanisms of which are adsorption (physical and/or chemical), pore blocking, deposition of a cake layer, and gel formation [74][75][76][77][78][79]. The extent of fouling, which stems from the nature of foulant-membrane interaction, is a complex function of the feed characteristics (e.g., foulant type, foulant concentration, and physicochemical properties of the foulants such as the functional groups, charge, size, and conformation [72,[80][81][82]), operating conditions (e.g., inadequate pretreatment, inadequate control of the hydrodynamics of the system, excessive flux, and low cross-flow velocity (in cross-flow systems) [72,[82][83][84]), and membrane properties (e.g., pore-size distribution, surface roughness, charge properties, and hydrophobicity [70,[85][86][87]). …”
Section: Fouling and Concentration Polarization In Submerged Hf Systemsmentioning
confidence: 99%
“…Membranes with sparse surface porosity can aggravate the effect of adsorption and fouling due to a large build-up of solute near the pores. (Fane & Fell, 1987) Upon increasing surface porosity, the solute accumulation will be spread more evenly, which will also decrease the fouling.…”
Section: Surface Porositymentioning
confidence: 99%
“…Three possible approaches have been utilised for the control of membrane fouling [29]. Application of hydrophilic and charged functional groups on the membrane surface can modify the behaviour to retard microorganisms and hydrophobic solutes.…”
Section: ) Feedwater Characteristicsmentioning
confidence: 99%
“…Generating permeate flux against time curves for different types of membranes in a VSEP system, data was shown to fit with a power law mode given by equation 1 This model was utilised to calculate k fouling indices at different vibrations [70]. A lower fouling indices corresponds to a reduced decline in initial permeate flux [29]. Lower fouling indices were observed when vibration was applied.…”
Section: Open Channel Bulk Fluid Flowmentioning
confidence: 99%