4.7 Article

New Chelate Resins Prepared with Direct Red 23 for Cd2+, Ni2+, Cu2+ and Pb2+ Removal

期刊

POLYMERS
卷 14, 期 24, 页码 -

出版社

MDPI
DOI: 10.3390/polym14245523

关键词

Amberlite XAD7HP; Amberlite IRA 402; ion exchange mechanism; pi-pi interactions; chelation; simultaneous enrichment; higher selectivity; cadmium; nickel; copper; lead

资金

  1. Ministry of Education and Research of Romania through Program Nucleu [PN 19 04 03 01]
  2. European Social Fund from the Sectoral Operational Programme Human Capital 2014-2020 [13530/16.06.2022, 153734]

向作者/读者索取更多资源

In this study, two chelate resins were prepared and used to remove Cd2+, Ni2+, Cu2+, and Pb2+ from aqueous solutions. The adsorption capacity of the resins was found to be independent of pH, and the XAD7HP resin showed a higher adsorption capacity compared to the IRA 402 (Cl-) resin. Both resins showed efficient M2+ removal, with the XAD7HP-DR 23 resin being more effective. The M2+ recovery from the chelate resins confirmed their sustainability. The results suggest that these chelate resins have great potential for water treatment applications.
In this paper, two chelate resins prepared by a simple procedure were used for the removal of Cd2+, Ni2+, Cu2+, and Pb2+ (M2+) from aqueous solutions. Amberlite IRA 402 strongly basic anion exchange resin in Cl- form (IRA 402 (Cl-) together with Amberlite XAD7HP acrylic ester co-polymer (XAD7HP) were functionalized with chelating agent Direct red 23 (DR 23). The chelate resins (IRA 402-DR 23 and XAD7HP-DR 23) were obtained in batch mode. The influence of interaction time, pH and the initial concentration of DR 23 solution was investigated using UV-Vis spectrometry. The time necessary to reach equilibrium was 90 min for both resins. A negligible effect of adsorption capacity (Q(e)) was obtained when the DR 23 solution was adjusted at a pH of 2 and 7.9. The Q(e) of the XAD7HP resin (27 mg DR 23/g) is greater than for IRA 402 (Cl-) (21 mg DR 23/g). The efficiency of chelating resins was checked via M2+ removal determined by the atomic adsorption spectrometry method (AAS). The M2+ removal by the IRA 402-DR 23 and XAD7HP-DR 23 showed that the latter is more efficient for this propose. As a consequence, for divalent ions, the chelated resins followed the selectivity sequence: Cd2+ > Cu2+ > Ni2+ > Pb2+. Additionally, Cd2+, Cu2+ and Ni2+ removal was fitted very well with the Freundlich model in terms of height correlation coefficient (R-2), while Pb2+ was best fitted with Langmuir model for IRA 402-DR 23, the Cu2+ removal is described by the Langmuir model, and Cd2+, Ni2+ and Pb2+ removal was found to be in concordance with the Freundlich model for XAD7HP-DR 23. The M2+ elution from the chelate resins was carried out using 2 M HCl. The greater M2+ recovery from chelating resins mass confirmed their sustainability. The chelate resins used before and after M2+ removal by Fourier transform infrared spectroscopy (FTIR) and scanning electron microscopy (SEM) analysis were evaluated.

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