SORPTION OF HEAVY METAL IONS ON A GRANULAR BENTONITE–TYRE PYROLYSIS CARBON SORBENT: EFFECT OF pH, KINETICS, FIXED-BED DYNAMICS AND REGENERATION

Article Metrics
Abstract Views 5
PDF Downloads 3
Authors
  • Taylakov Utkir Tahirovich UZ

    Navoi State University of Mining and Technologies, Navoi, Uzbekistan
  • Jo‘rayev Shoxruh To‘lqinovich UZ

    Navoi State University of Mining and Technologies, Navoi, Uzbekistan
Keywords:
heavy metals granular sorbent tyre pyrolysis char bentonite sorption kinetics thermodynamics fixed-bed column regeneration
Abstract
Waste tyres and metal-bearing industrial effluents are two linked environmental problems in mining regions. This study evaluated a granular sorbent made from bentonite and the carbon-containing residue of waste tyre pyrolysis (G-BU(opt), activated at 750 °C) for the removal of Fe(III), Cu(II), Zn(II), Ni(II), Pb(II), Cd(II) and Cr(VI) from aqueous solutions. Batch experiments examined the effect of initial pH (1.5–6.0), contact time (1–1440 min), temperature (293–323 K) and competition in an equimolar mixture; fixed-bed column tests and five sorption–desorption cycles were carried out with Cu(II). Cation removal increased from 6.24–18.53 % at pH 1.5 to 71.68–89.45 % at pH 6.0, which corresponds to 35.8–44.7 mg/g, whereas Cr(VI) removal reached a maximum of 34.56 % at pH 4.0. The pseudo-second-order model described the kinetics better than the pseudo-first-order model (adjusted R² of 0.9956–0.9991 and 0.9154–0.9513, respectively). Sorption was spontaneous (ΔG° from −2.57 to −3.94 kJ/mol) and endothermic (ΔH° from +5.36 to +6.09 kJ/mol). In the equimolar mixture the ratio of multi- to single-component uptake decreased in the order Pb(II) 0.86 > Cu(II) 0.77 > Zn(II) 0.69 > Cd(II) 0.67 > Ni(II) 0.65. In a 6 cm bed at 4 mL/min and C₀ = 100 mg/L, the Cu(II) breakthrough and exhaustion times were 15 and 65 min. After five regeneration cycles with 0.1 mol/L HCl the sorbent retained 75.38 % of its initial Cu(II) capacity.
References

[1] F. Fu and Q. Wang, “Removal of heavy metal ions from wastewaters: A review,” J. Environ. Manage., vol. 92, no. 3, pp. 407–418, 2011, doi: 10.1016/j.jenvman.2010.11.011.

[2] H. Rutto, T. Seidigeng, and L. Malise, “Adsorption of lead ions onto chemically activated carbon from waste tire char and optimization of the process using response surface methodology,” Arch. Environ. Prot., vol. 45, no. 4, pp. 92–103, 2019, doi: 10.24425/aep.2019.130245.

[3] S. M. H. Shah et al., “Mechanistic insights into heavy metal adsorption on pyrolytic char from waste tires using experimental and DFT approaches,” Discover Water, vol. 5, no. 1, Art. no. 107, 2025, doi: 10.1007/s43832-025-00314-x.

[4] M. I. Inyang et al., “A review of biochar as a low-cost adsorbent for aqueous heavy metal removal,” Crit. Rev. Environ. Sci. Technol., vol. 46, no. 4, pp. 406–433, 2016, doi: 10.1080/10643389.2015.1096880.

[5] B. M. Babić, S. K. Milonjić, M. J. Polovina, and B. V. Kaludierović, “Point of zero charge and intrinsic equilibrium constants of activated carbon cloth,” Carbon, vol. 37, pp. 477–481, 1999, doi: 10.1016/S0008-6223(98)00216-4.

[6] H. Patel, “Fixed-bed column adsorption study: a comprehensive review,” Appl. Water Sci., vol. 9, no. 3, Art. no. 45, 2019, doi: 10.1007/s13201-019-0927-7.

[7] S. Lata, P. K. Singh, and S. R. Samadder, “Regeneration of adsorbents and recovery of heavy metals: a review,” Int. J. Environ. Sci. Technol., vol. 12, no. 4, pp. 1461–1478, 2015, doi: 10.1007/s13762-014-0714-9.

[8] Sh. T. Jo‘rayev, “Technologies for obtaining and applying ingredients based on low-temperature thermal processing of vulcanized rubber industry waste,” D.Sc. dissertation, Navoi State Univ. of Mining and Technologies, Navoi, Uzbekistan, 2025 (in Uzbek).

[9] Drinking Water. Determination of Elements Content by Atomic Spectrometry Methods, GOST 31870-2012, 2012 (in Russian).

[10] S. Lagergren, “Zur Theorie der sogenannten Adsorption gelöster Stoffe,” Kungliga Svenska Vetenskapsakademiens Handlingar, vol. 24, no. 4, pp. 1–39, 1898.

[11] Y. S. Ho and G. McKay, “Pseudo-second order model for sorption processes,” Process Biochem., vol. 34, no. 5, pp. 451–465, 1999, doi: 10.1016/S0032-9592(98)00112-5.

[12] J.-P. Simonin, “On the comparison of pseudo-first order and pseudo-second order rate laws in the modeling of adsorption kinetics,” Chem. Eng. J., vol. 300, pp. 254–263, 2016, doi: 10.1016/j.cej.2016.04.079.

[13] E. C. Lima, A. Hosseini-Bandegharaei, J. C. Moreno-Piraján, and I. Anastopoulos, “A critical review of the estimation of the thermodynamic parameters on adsorption equilibria. Wrong use of equilibrium constant in the Van’t Hoof equation for calculation of thermodynamic parameters of adsorption,” J. Mol. Liq., vol. 273, pp. 425–434, 2019, doi: 10.1016/j.molliq.2018.10.048.

[14] H. N. Tran, S.-J. You, A. Hosseini-Bandegharaei, and H.-P. Chao, “Mistakes and inconsistencies regarding adsorption of contaminants from aqueous solutions: A critical review,” Water Res., vol. 120, pp. 88–116, 2017, doi: 10.1016/j.watres.2017.04.014.

How to Cite

Tahirovich, T. U., & To‘lqinovich, J. S. (2025). SORPTION OF HEAVY METAL IONS ON A GRANULAR BENTONITE–TYRE PYROLYSIS CARBON SORBENT: EFFECT OF pH, KINETICS, FIXED-BED DYNAMICS AND REGENERATION. Innovative: International Multidisciplinary Journal of Applied Technology (2995-486X), 3(10), 159-165. https://doi.org/10.51699/ex8hya54