Optimization of arsenic removal from water using novel renewable adsorbents derived from orange peels

• TiO 2 impacted orange peel activated carbon (ACOP-TiO 2 ) physicochemical properties. • ACOP-TiO 2 adsorption capacity for arsenic (As) reached 10.91 mg/g. • Optimal condition: pH = 4.2, As initial concentration = 50 mg/L, adsorbent dose = 3.3 g/L. • Pseudo-2nd-order kinetic and Freundlich isotherm models best describe As adsorption. • Thermodynamic studies revealed a spontaneous and endothermic process. This study developed activated carbon from orange peels (ACOP) and modified ACOP with titanium dioxide (TiO 2 ) (ACOP-TiO 2 ), focusing on optimizing the adsorption capacity of ACOP-TiO 2 for arsenic removal from water. The developed adsorbent (ACOP-TiO 2 ) was prepared and characterized by Scanning electron microscopy (SEM), Energy dispersive X-ray analysis (EDS), Fourier transform infrared spectroscopy (FTIR), X-ray diffraction (XRD), surface area analysis, and elemental analysis. The Brunauer-Emmett-Teller (BET) test demonstrated that the modification increased the surface area of ACOP-TiO 2 by 2.55 times greater than ACOP. Adsorption experiments were conducted using synthetic aqueous solutions of arsenic (As(V)), and the response surface methodology (RSM) incorporating central composite design (CCD) was employed for experimental optimization. The results indicated that ACOP-TiO 2 demonstrated efficient arsenic removal, with optimal pH identified at approximately 4.2. Increasing adsorbent dosage (0.025–0.4 g in 50 mL solution, corresponding to 0.5–8 g L -1 ) positively influenced adsorption efficiency, while initial arsenic concentration (10–60 mg L -1 ) directly correlated with adsorbent capacity, with a predicted optimum concentration of 50 mg L -1 . Contact time (0.4–6 h) exhibited minimal impact on adsorbent capacity within the experimental timeframe. Under the conditions of pH 4.2, an initial arsenic concentration of 50 mg L -1 , an adsorbent dose of 3.3 g L -1 (0.165 g adsorbent/50 mL solution), and a contact time of 4.8 h, the maximum adsorbent capacity in arsenic removal for ACOP-TiO 2 was 10.91 mg g −1 . The intra-particle diffusion kinetic model and Temkin isotherm best described arsenic adsorption onto ACOP-TiO 2 . This research contributes valuable insights into utilizing agricultural waste for water treatment, offering a sustainable and economical solution for arsenic removal.

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Publication Details

Journal
Waste Management Bulletin
Published
2025-02-28
DOI
https://doi.org/10.1016/j.wmb.2025.02.006
Citations
2
Primary Topic
Arsenic contamination and mitigation
Type
article
Field-Weighted Citation Impact
1.72

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article

Optimization of arsenic removal from water using novel renewable adsorbents derived from orange peels

Sohrab Zendehboudi, Carlos Bazán, Noori M. Cata Saady, Roya Sadat Neisan
2 citations
Waste Management Bulletin
Arsenic contamination and mitigation
1.72
article

Optimization of arsenic removal from water using novel renewable adsorbents derived from orange peels

Sohrab Zendehboudi, Carlos Bazán, Noori M. Cata Saady, Roya Sadat Neisan
article en
2 citations

Abstract

• TiO 2 impacted orange peel activated carbon (ACOP-TiO 2 ) physicochemical properties. • ACOP-TiO 2 adsorption capacity for arsenic (As) reached 10.91 mg/g. • Optimal condition: pH = 4.2, As initial concentration = 50 mg/L, adsorbent dose = 3.3 g/L. • Pseudo-2nd-order kinetic and Freundlich isotherm models best describe As adsorption. • Thermodynamic studies revealed a spontaneous and endothermic process. This study developed activated carbon from orange peels (ACOP) and modified ACOP with titanium dioxide (TiO 2 ) (ACOP-TiO 2 ), focusing on optimizing the adsorption capacity of ACOP-TiO 2 for arsenic removal from water. The developed adsorbent (ACOP-TiO 2 ) was prepared and characterized by Scanning electron microscopy (SEM), Energy dispersive X-ray analysis (EDS), Fourier transform infrared spectroscopy (FTIR), X-ray diffraction (XRD), surface area analysis, and elemental analysis. The Brunauer-Emmett-Teller (BET) test demonstrated that the modification increased the surface area of ACOP-TiO 2 by 2.55 times greater than ACOP. Adsorption experiments were conducted using synthetic aqueous solutions of arsenic (As(V)), and the response surface methodology (RSM) incorporating central composite design (CCD) was employed for experimental optimization. The results indicated that ACOP-TiO 2 demonstrated efficient arsenic removal, with optimal pH identified at approximately 4.2. Increasing adsorbent dosage (0.025–0.4 g in 50 mL solution, corresponding to 0.5–8 g L -1 ) positively influenced adsorption efficiency, while initial arsenic concentration (10–60 mg L -1 ) directly correlated with adsorbent capacity, with a predicted optimum concentration of 50 mg L -1 . Contact time (0.4–6 h) exhibited minimal impact on adsorbent capacity within the experimental timeframe. Under the conditions of pH 4.2, an initial arsenic concentration of 50 mg L -1 , an adsorbent dose of 3.3 g L -1 (0.165 g adsorbent/50 mL solution), and a contact time of 4.8 h, the maximum adsorbent capacity in arsenic removal for ACOP-TiO 2 was 10.91 mg g −1 . The intra-particle diffusion kinetic model and Temkin isotherm best described arsenic adsorption onto ACOP-TiO 2 . This research contributes valuable insights into utilizing agricultural waste for water treatment, offering a sustainable and economical solution for arsenic removal.

Waste Management BulletinVol. 3(2)
Memorial University of Newfoundland (CA)
Mitacs, Memorial University of Newfoundland, Natural Sciences and Engineering Research Council of Canada
Clean water and sanitation
Openalex Percentile: Top 19%
Arsenic contamination and mitigation
1.72
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