2018
DOI: 10.1016/j.chemosphere.2017.10.005
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Effect of pore structure on the removal of clofibric acid by magnetic anion exchange resin

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Cited by 21 publications
(7 citation statements)
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“…For the removal of pharmaceuticals and acidic drugs such as CA metabolites, several physicochemical water treatment procedures were investigated, e.g., coagulation, adsorption through granular activated carbon [12,13], sedimentation, or filtration [14]. However, the main disadvantage of these techniques is that they transfer the pollutant from one phase to another but do not completely remove it through a mineralization mechanism.…”
Section: Introductionmentioning
confidence: 99%
“…For the removal of pharmaceuticals and acidic drugs such as CA metabolites, several physicochemical water treatment procedures were investigated, e.g., coagulation, adsorption through granular activated carbon [12,13], sedimentation, or filtration [14]. However, the main disadvantage of these techniques is that they transfer the pollutant from one phase to another but do not completely remove it through a mineralization mechanism.…”
Section: Introductionmentioning
confidence: 99%
“…Removing these contaminants from industrial wastewaters before effluents are discharged into the aquatic environment is obviously necessary. Various methods, such as biological processes [2], ultrasound [3], active carbon adsorption [4], ozone treatment [5], coagulation/flocculation [6], and ion exchange resin [7,8] and ion exchange membrane adsorption methods [9], have been investigated in an attempt to remediate dye-containing wastewaters. However, these methods are not always efficient and economical enough, so new alternative technologies that rely on low-cost materials are mandatory to solve the issues related to dye-containing wastewaters [10].…”
Section: Introductionmentioning
confidence: 99%
“…Hence, the higher the functional group density of a resin, the higher the PTSA adsorption capacity. Nevertheless, the adsorption amount of resins significantly decreased with increase in the initial concentration of Na 2 SO 4 , suggesting that there was a strong competitive effect between the sulfate radical and the PTSA anion [24]. When the Na 2 SO 4 content in the solution increased to 1%, it was found that the adsorption amount order completely reversed to SD5 < SD4 < SD3 < SD2 < SD1.…”
Section: Effect Of So4 2− On Adsorption and Selectivity Of Ptsamentioning
confidence: 94%
“…However, the results were not always satisfactory because of lower selectivity of these commercial resins for ASAs to inorganic anions, especially sulfate, which is often present in ASA waste streams at a high level [19,20]. Therefore, many efforts have been made by scientists to modify weak-base anion exchangers to improve their adsorption capacity and selectivity, mainly focusing on the optimization of functional groups [11,12,[21][22][23] and the adjustment of the resin matrix structure [24]. It is worth noting that the functional group density of an adsorbent also affects its adsorption selectivity [25,26].…”
Section: Introductionmentioning
confidence: 99%