2009
DOI: 10.1016/j.desal.2007.11.077
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The removal of zinc from synthetic wastewaters by micellar-enhanced ultrafiltration: statistical design of experiments

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Cited by 146 publications
(43 citation statements)
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“…The Cr(VI) removal by these techniques is conducted by electrostatic interactions between the contaminant and the membrane surface or by the molecular size. Therefore, the porous size of the membranes is an important factor in preventing the dissolved metallic ions or the low molecular weight complexes from passing through the membrane (Landaburu-Aguirre et al 2009). The ionic exchange process uses natural or synthetic resins that have the specific capacity to exchange their ions with the heavy metals that are present in the wastewater (Kang et al 2007), but the last ones are commonly preferred due to their ability to eliminate almost all of the metallic ions (Alyüz and Veli 2009).…”
Section: Removal Techniques For Cr(vi)mentioning
confidence: 99%
“…The Cr(VI) removal by these techniques is conducted by electrostatic interactions between the contaminant and the membrane surface or by the molecular size. Therefore, the porous size of the membranes is an important factor in preventing the dissolved metallic ions or the low molecular weight complexes from passing through the membrane (Landaburu-Aguirre et al 2009). The ionic exchange process uses natural or synthetic resins that have the specific capacity to exchange their ions with the heavy metals that are present in the wastewater (Kang et al 2007), but the last ones are commonly preferred due to their ability to eliminate almost all of the metallic ions (Alyüz and Veli 2009).…”
Section: Removal Techniques For Cr(vi)mentioning
confidence: 99%
“…In electrochemical treatment the high flow real plating wastewater (Bohdziewicz, 2000) The anionic-based resin was used in hydroxide form in the column and 100% removal of chromium (VI) was obtained. Other ion exchange resin, Ambersep 132 was used to recover chromic acid from synthetic plating solution in four steps (Landaburu-Aguirre et al, 2009) In the first step, ion-exchange resin captures the chromic acid, and in the second step, it is reacted with sodium hydroxide solution and transformed into sodium chromate In the third step, cationic ion-exchange resin was used to again transfer the sodium chromate into chromic acid, and in the final fourth step, the ion-exchange resin reacts with hydrochloric acid (HCL) to regenerate it again This fourth step is shown to be effective and also accomplished to provide continuous chromic acid. Solventimpregnated resin (SIR) with aliquot 336 is prepared by (Kabay) (Kabay, Arda, Saha, & Streat, 2003) and batch adsorption studies will be done.…”
Section: Electrocoagulation For Nickel (Ii)mentioning
confidence: 99%
“…Among various existing processes there are: ion exchange 2 , the chemical precipitation 3 and ultrafiltration 4 . These methods are not always effective, and usuallyhave high cost and generate waste, thus, requiring a further stage of treatment.…”
Section: Introductionmentioning
confidence: 99%