“…However, as discussed in detail later, the crude oil in this study was considered non-polar, so the DLVO model was more applicable. In applying the DLVO model, membrane was treated as a flat surface and oil droplets were approximated as perfect spheres and point charges, consistent with previous studies (Aimar and Bacchin 2010, Bacchin et al 1995, Bacchin et al 2002, Brant and Childress 2002, Hoek et al 2003, Muthu et al 2014. 8…”
The effects of inorganic salts and organic hydrocarbons on membrane fouling are often investigated independently. However, in many cases, these foulants are commonly found together, and such mixtures are rarely the subject of fouling studies. In this study, crude oil-in-water emulsions were formulated at three different added NaCl concentrations, 0, 10 and 10 M. Surface properties, such as surface tension and surface charge, of these emulsions and a poly(vinylidene fluoride) (PVDF) microfiltration (MF) membrane were characterized. The Derjaguin-Landau-Verwey-Overbeek (DLVO) model was utilized to simulate membrane-oil droplet and oil layer-oil droplet surface interactions. The DLVO model qualitatively predicted increasing fouling propensity with increasing emulsion salt concentration. The PVDF MF membrane was challenged with crude oil-in-water emulsions in constant permeate flux crossflow fouling tests to characterize the fouling propensity of the various emulsions, and the results were consistent with the model predictions.
“…However, as discussed in detail later, the crude oil in this study was considered non-polar, so the DLVO model was more applicable. In applying the DLVO model, membrane was treated as a flat surface and oil droplets were approximated as perfect spheres and point charges, consistent with previous studies (Aimar and Bacchin 2010, Bacchin et al 1995, Bacchin et al 2002, Brant and Childress 2002, Hoek et al 2003, Muthu et al 2014. 8…”
The effects of inorganic salts and organic hydrocarbons on membrane fouling are often investigated independently. However, in many cases, these foulants are commonly found together, and such mixtures are rarely the subject of fouling studies. In this study, crude oil-in-water emulsions were formulated at three different added NaCl concentrations, 0, 10 and 10 M. Surface properties, such as surface tension and surface charge, of these emulsions and a poly(vinylidene fluoride) (PVDF) microfiltration (MF) membrane were characterized. The Derjaguin-Landau-Verwey-Overbeek (DLVO) model was utilized to simulate membrane-oil droplet and oil layer-oil droplet surface interactions. The DLVO model qualitatively predicted increasing fouling propensity with increasing emulsion salt concentration. The PVDF MF membrane was challenged with crude oil-in-water emulsions in constant permeate flux crossflow fouling tests to characterize the fouling propensity of the various emulsions, and the results were consistent with the model predictions.
“…6b). Aimar et al [24] attributed this flux stabilization to the filtration under critical flux. At this flux, back transport of nanoparticles due to diffusion and electrostatic repulsion between nanoparticles is equal to convective transport towards the membrane surface.…”
Section: Influence Of Nanoparticle Concentrationmentioning
confidence: 97%
“…However, for less stable nanoparticle suspensions, an increase in the nanoparticle concentration on the membrane surface can most likely result in local-near membrane surface clustering and aggregation of nanoparticles [24]. This lower nanoparticle stability promotes faster pore blockage, followed by the formation of a denser and less permeable cake layer.…”
“…Membrane fouling with colloids and biocolloids is usually known as an inherent problem in membrane processes and makes them less competitive [43]. In this event, solute or particles deposit onto a membrane surface or into membrane pores.…”
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