New Chelating Ion-Exchange Resin Synthesized via the Cyclopolymerization Protocol and Its Uptake Performance for Metal Ion Removal

2015 ◽  
Vol 54 (40) ◽  
pp. 9689-9698 ◽  
Author(s):  
Shaikh A. Ali ◽  
Izzat W. Kazi ◽  
Nisar Ullah
2016 ◽  
Vol 13 (3) ◽  
pp. 478 ◽  
Author(s):  
Sébastien Leguay ◽  
Peter G. C. Campbell ◽  
Claude Fortin

Environmental context The lanthanides are a group of heavy elements (from lanthanum to lutetium) increasingly used in many electronic consumer products and little is known about their environmental mobility and toxicity. In natural systems, these elements will bind to natural organic matter but metal toxicity is usually defined by the free metal ion concentration. Here, we propose a method based on sample equilibration with an ion-exchange resin to measure the free lanthanide ion concentration in the presence of natural organic matter. Abstract An ion-exchange technique that employs a polystyrene sulphonate ion-exchange resin was developed for determining environmentally relevant free-ion concentrations of Ce, Eu, La and Nd. Owing to the high affinity of rare earth elements (REE) for the selected resin, this method requires the addition of an inert salt to increase the concentration of the counter-ions (i.e. cations that are exchanged with REE bound to the resin). The use of a batch equilibration approach to calibrate the resin allowed the implementation of the ion-exchange technique at reasonably low ionic strength (I = 0.1M). Several ligands were used to test the selectivity of the method, which proved to be highly selective for the free metal ion in presence of the tested cationic and anionic complexes (REE–nitrate, REE–malic acid and REE–nitrilotriacetic acid systems) and operational for very low proportions of REE3+, owing to the strong REE–resin interactions. The ion-exchange technique was also implemented to determine [Eu]inorg in the presence of natural humic matter (Suwannee River Humic Acid) and the results were compared with those obtained using equilibrium dialysis and those calculated with chemical equilibrium models. At pH 4.00, the measured [Eu]inorg values were in fairly good agreement with those predicted with the Windermere Humic Aqueous Model and Stockholm Humic Model, whereas the Non-Ideal Competitive Absorption model appeared to underestimate the [Eu]inorg. However, the inorganic europium concentrations were strongly underestimated (4 < [Eu]inorg, IET/[Eu]inorg, calc < 18) with the three prediction models at higher pH (5.3 and 6.2).


2008 ◽  
Vol 142 (6) ◽  
pp. 962-970 ◽  
Author(s):  
Masahiro Takeyama ◽  
Keiji Nogami ◽  
Masahiro Okuda ◽  
Yoshihiko Sakurai ◽  
Tomoko Matsumoto ◽  
...  

2020 ◽  
Vol 30 (4) ◽  
pp. 276-281
Author(s):  
Kyung-Han Lee ◽  
Bo-Min Kil ◽  
Cheol-Hwi Ryu ◽  
Gab-Jin Hwang

2014 ◽  
Vol 955-959 ◽  
pp. 2230-2233 ◽  
Author(s):  
Yong Gang Zeng ◽  
Long Li

This paper used the ion exchange resin method to treat the heavy metal ion Cu2+ of a chemical wastewater and studied the flow velocity, pH and the temperature’s effect on Cu2+ removal effect by macroporous strongly acidic styrene type cation exchange resin D001. The results shown that: when the flow velocity was 1.5 mL/min, pH was 6.0 and the temperature was 30°C, the removal rate of Cu2+ by D001 reached 99.8%. The chemical wastewater could achieve the wastewater’s discharge standard.


Ionics ◽  
2019 ◽  
Vol 25 (8) ◽  
pp. 3847-3857 ◽  
Author(s):  
M. Nemati ◽  
S. M. Hosseini ◽  
F. Parvizian ◽  
N. Rafiei ◽  
B. Van der Bruggen

Desalination ◽  
2008 ◽  
Vol 232 (1-3) ◽  
pp. 3-10 ◽  
Author(s):  
Jaya Mohandas ◽  
T. Kumar ◽  
S.K. Rajan ◽  
S. Velmurugan ◽  
S.V. Narasimhan

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