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. 2025 Aug 11.
doi: 10.1039/d5na00409h. Online ahead of print.

Copper ferrite-graphene oxide catalyst for enhanced peroxymonosulfate activation and pollutant degradation

Affiliations

Copper ferrite-graphene oxide catalyst for enhanced peroxymonosulfate activation and pollutant degradation

Imane Sebah et al. Nanoscale Adv. .

Abstract

In this study, a magnetic nanocomposite of copper ferrite (CuFe2O4) supported on reduced graphene oxide (rGO) was synthesized via a solvothermal method and applied as a catalyst for the activation of peroxymonosulfate (PMS) to degrade Orange G (OG) dye in aqueous solution. The structure and morphology of the catalyst were thoroughly characterized using XRD, FTIR, SEM, STEM, and nitrogen adsorption-desorption analyses. The rGO/CuFe2O4 composite demonstrated superior catalytic performance, achieving 90.8% OG removal within 60 minutes, attributed to its enhanced surface area, efficient radical generation, and strong interaction between rGO and CuFe2O4. The system exhibited high activity across a wide pH range, significant mineralization (78% TOC removal), and good recyclability over four cycles. The catalyst also effectively degraded other dyes including rhodamine B (78%), methylene blue (86%), and methyl orange (89%) under similar conditions. These findings suggest that rGO/CuFe2O4 is a promising, reusable catalyst for advanced oxidation processes in wastewater treatment.

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Conflict of interest statement

There are no conflicts to declare.

Figures

Fig. 1
Fig. 1. Schematic illustration of the hydrothermal synthesis of rGO/CuFe2O4 nanocomposite.
Fig. 2
Fig. 2. XRD patterns of CuFe2O4 and rGO/CuFe2O4 samples.
Fig. 3
Fig. 3. FTIR spectra of graphene oxide (GO), CuFe2O4 and rGO/CuFe2O4 samples.
Fig. 4
Fig. 4. Nitrogen adsorption/desorption isotherm of CuFe2O4 and rGO/CuFe2O4 samples.
Fig. 5
Fig. 5. SEM images of (a) CuFe2O4 and (b) rGO/CuFe2O4 samples.
Fig. 6
Fig. 6. STEM images of (a and b) CuFe2O4 and (c and d) rGO/CuFe2O4 samples.
Fig. 7
Fig. 7. Particle size distribution analysis of (a) CuFe2O4 and (b) rGO/CuFe2O4.
Fig. 8
Fig. 8. (a) Removal efficiency of OG in different system, Reaction conditions: [catalyst] = 0.2 g L−1; [PMS] = 2 mM; [OG] = 50 mg L−1; initial pH without adjustment. Effects of operating parameters on OG degradation (b) PMS dosage, (c) catalyst dosage, and (d) various pH conditions.
Fig. 9
Fig. 9. pH point zero charge (pHPZC) of rGO/CuFe2O4.
Fig. 10
Fig. 10. (a) Degradation of various organic dyes using the rGO/CuFe2O4–PMS system. (b) Discoloration and mineralization (TOC removal) of OG at different reaction times under optimal conditions. Reaction conditions: [catalyst] = 0.2 g L−1; [PMS] = 2 mM; [OG] = 50 mg L−1, [BM] = 10 mg L−1; [RhB] = 10 mg L−1; [MO] = 10 mg L−1.
Fig. 11
Fig. 11. Recycling tests of the rGO/CuFe2O4 catalyst; reaction conditions: [catalyst] = 0.2 g L−1; [PMS] = 2 mM; [OG] = 50.
Fig. 12
Fig. 12. The effect of scavengers on OG degradation using different scavengers.
Fig. 13
Fig. 13. Proposed mechanism of orange G degradation in the rGO–CuFe2O4/PMS system.

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