2016
DOI: 10.1016/j.jece.2016.08.024
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Adsorption of lanthanides and scandium ions by silica sol-gel material doped with novel bifunctional ionic liquid, trioctylmethylammonium 1-phenyl-3-methyl-4-benzoyl-5-onate

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Cited by 28 publications
(9 citation statements)
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“…For example, Ma et al [12] evaluated the sorption rate of 0.0528 g mg −1 min −1 for Sc(III) on lysinefunctionalized mesoporous material (initial metal concentration 20 mg dm −3 , adsorbent dose = 0.25 g dm −3 ) and the value of 0.00101 g mg −1 min −1 was reported for CNTs modified with activated carbon [18]. On the other hand, Turanov et al [13] reported the kinetic sorption rate for Sc(III) on silica doped with trioctylmethylammonium 1-phenyl-3-methyl-4-benzoyl-5-onate ionic liquid equals to 8.64 g mg −1 min −1 (initial concentration of 1.35 mg dm −3 , V/m = 5 g dm −3 ). However, for that sorbent, very low (0.27 mg g −1 ) sorption capacity was obtained [13].…”
Section: Kinetic Model Equation Parametersmentioning
confidence: 99%
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“…For example, Ma et al [12] evaluated the sorption rate of 0.0528 g mg −1 min −1 for Sc(III) on lysinefunctionalized mesoporous material (initial metal concentration 20 mg dm −3 , adsorbent dose = 0.25 g dm −3 ) and the value of 0.00101 g mg −1 min −1 was reported for CNTs modified with activated carbon [18]. On the other hand, Turanov et al [13] reported the kinetic sorption rate for Sc(III) on silica doped with trioctylmethylammonium 1-phenyl-3-methyl-4-benzoyl-5-onate ionic liquid equals to 8.64 g mg −1 min −1 (initial concentration of 1.35 mg dm −3 , V/m = 5 g dm −3 ). However, for that sorbent, very low (0.27 mg g −1 ) sorption capacity was obtained [13].…”
Section: Kinetic Model Equation Parametersmentioning
confidence: 99%
“…On the other hand, Turanov et al [13] reported the kinetic sorption rate for Sc(III) on silica doped with trioctylmethylammonium 1-phenyl-3-methyl-4-benzoyl-5-onate ionic liquid equals to 8.64 g mg −1 min −1 (initial concentration of 1.35 mg dm −3 , V/m = 5 g dm −3 ). However, for that sorbent, very low (0.27 mg g −1 ) sorption capacity was obtained [13]. Furthermore, intra-particle diffusion model was used to investigate the contribution of various steps involved in the adsorption process such as intraparticle and film diffusions.…”
Section: Kinetic Model Equation Parametersmentioning
confidence: 99%
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“…The reported adsorbents include carbons activated by KOH, HNO 3 H 3 PO 4 and ZnCl 2 , 17 olive wood biosorbents, 18 UiO-66-NH 2 , 19 glycidyl methacrylate graed cotton cellulose, 20 yellow bentonite, 21 XAD-4 resin, 22 activated carbon bers, 23 layered double hydroxides and their calcined products, 24 carbon nanospheres, 25 date seeds 26 and active carbon. 27 In recent years, ionic liquid-modied silicas (IL-silicas) as adsorbents have been widely used to remove Cu(II), Fe(III), Mn (II) and Ni(II), 28 Pb(II), [29][30][31] Cr(III,VI), [32][33][34] lanthanides and scandium ions, 35 oxymatrine, 36 bovine serum albumin, 37 racemic amino acids, 28 thiophenic sulfur compounds, 38 anionic dye, 39,40 dibenzothiophene 41 and phenolic compounds (4-chlorophenol, 42 polyphenols, 43 phenolic acids, 44 naphthols, 45 bisphenol A 46 and 2,4-DNP [47][48][49] ). To elucidate the relation between the structure of IL-silicas and their adsorption performance for phenolic compounds, a series of IL-silicas were designed by varying substituents, the functional groups of the imidazolium ring, counter ions and silane-coupling agents.…”
Section: Introductionmentioning
confidence: 99%