Boron Sorption on Selected NMDG Resins: Diffusion Kinetics and Equilibrium Modeling

Authors

  • Yousef SWESI Department of Chemical Engineering, Faculty of Engineering, University of Tripoli Author
  • Assma ALHARATI Department of Mining Engineering, Faculty of Engineering, University of Tripoli Author
  • Catherine CHARCOSSET Laboratory of Automation, Process Engineering and Pharmaceutical Engineering, University Claude Bernard, France Author
  • Koffi FIATY Laboratory of Automation, Process Engineering and Pharmaceutical Engineering, University Claude Bernard, France Author

DOI:

https://doi.org/10.66411/jer.v41i2.145

Keywords:

Boron Elimination, Resin, Ion-Exchange, Water Desalination

Abstract

Boron removal from water remains a significant challenge in desalination and wastewater treatment due to boron's low ionization potential and high solubility. This study characterizes the sorption performance of selective N-methyl-D-glucamine (NMDG) ion-exchange resins in a batch system. Equilibrium and kinetic sorption parameters were determined through batch experiments to characterize the dominant mass-transfer mechanisms governing uptake on three NMDG-bearing commercial resins Amberlite IRA743, Purolite S108, and Diaion CRB05 over a range of particle-size fractions. Equilibrium data fit best to the Langmuir isotherm, indicating monolayer sorption behavior. Kinetic analysis using the Shrinking Core Model and the Homogeneous Particle Diffusion Model confirmed that boron uptake is primarily governed by intraparticle diffusion rather than by external film resistance or surface chemical reactions. Although the pseudo-second-order model yielded a high statistical correlation with the batch data, it is interpreted as a macro-level empirical description rather than as mechanistic evidence of a rate-limiting reaction. A diffusion-based "Dp" model, coupling a material balance with the HPDM, was developed and validated against experimental concentration profiles for all tested resins. The model showed good agreement, providing physically meaningful estimates of the effective diffusion coefficient (Deff) and external mass transfer coefficient (K). These findings establish a rigorous mechanistic foundation for the design and scale-up of boron sorption processes

References

[1] A. Imbernón-Mulero et al., “Ion exchange resins to reduce boron in desalinated seawater for irrigation in southeastern Spain,” Agronomy, vol. 12, no. 6, p. 1389, Jun. 2022. DOI: https://doi.org/10.3390/agronomy12061389

[2] M. Figueira, M. Fernández de Labastida, C. Valderrama, and M. Reig, “Boron separation and concentration from pre-treated seawater reverse osmosis brines by selective ion-exchange resins and electrodialysis,” Chem. Eng. J., vol. 463, p. 142310, May 2023.

[3] N. Najid et al., “Comparison of different membrane technologies for boron removal from seawater,” in Membrane Technologies for Heavy Metal Removal from Water, London, UK: Taylor & Francis, 2024. DOI: https://doi.org/10.1201/9781003326281-10

[4] T. Mathialagan and T. Viraraghavan, “Adsorption of cadmium from aqueous solutions by perlite,” J. Hazard. Mater., vol. 94, no. 3, pp. 291–303, Sep. 2002. DOI: https://doi.org/10.1016/S0304-3894(02)00084-5

[5] İ. Yılmaz İpek, N. Kabay, and M. Yüksel, “Modeling of fixed bed column studies for removal of boron from geothermal water by selective chelating ion exchange resins,” Desalination, vol. 310, pp. 151–157, Feb. 2013. DOI: https://doi.org/10.1016/j.desal.2012.10.009

[6] T. E. Köse and N. Öztürk, “Boron removal from aqueous solutions by ion-exchange resin: Column sorption–elution studies,” J. Hazard. Mater., vol. 152, no. 2, pp. 744–749, Apr. 2008. DOI: https://doi.org/10.1016/j.jhazmat.2007.07.041

[7] N. Darwish, B. Kochkodan, and N. Hilal, “Boron removal from water with fractionized Amberlite IRA743 resin,” Desalination, vol. 370, pp. 1–6, Oct. 2015.

[8] A. B. Koltuniewicz and K. Bezak, “Efficiency of membrane-sorption integrated processes,” J. Membr. Sci., vol. 239, no. 1, pp. 129–141, Aug. 2004. DOI: https://doi.org/10.1016/j.memsci.2004.02.037

[9] R. G. Holdich, I. W. Cumming, and S. Perni, “Boron Mass Transfer During Seeded Microfiltration,” Chem. Eng. Res. Des., vol. 84, no. 1, pp. 60–68, Jan. 2006. DOI: https://doi.org/10.1205/cherd.05015

[10] N. Kabay et al., “Removal of boron from seawater by selective ion exchange resins,” React. Funct. Polym., vol. 67, no. 12, pp. 1643–1650, Dec. 2007. DOI: https://doi.org/10.1016/j.reactfunctpolym.2007.07.033

[11] P. R. Santander et al., “Removal of boron from geothermal water by a novel boron selective resin,” Desalination, vol. 310, pp. 102–108, Feb. 2013. DOI: https://doi.org/10.1016/j.desal.2012.08.026

[12] L. Montastruc, I. Nikov, P. Floquet, and S. Domenech, “Integrated process for production of surfactin (III) Modeling of adsorption column,” Chin. J. Chem. Eng., vol. 19, no. 3, pp. 357–364, Jun. 2011. DOI: https://doi.org/10.1016/S1004-9541(09)60221-4

[13] N. Kabay et al., “Removal and recovery of boron from geothermal wastewater by selective ion exchange resins. I. Laboratory tests,” React. Funct. Polym., vol. 60, pp. 163–170, Jul. 2004. DOI: https://doi.org/10.1016/j.reactfunctpolym.2004.02.020

[14] C. Farran et al., “Kinectics of polycyclic aromatic hydrocarbons removal using hyper-cross-linked polymeric sorbents Macronet Hypersol MN200,” React. Funct. Polym., vol. 67, no. 12, pp. 1515–1529, Dec. 2007. DOI: https://doi.org/10.1016/j.reactfunctpolym.2007.07.020

[15] N. B. Darwish, V. Kochkodan, and N. Hilal, "Boron removal from water with fractionized Amberlite IRA743 resin," Desalination, vol. 370, pp. 1–6, Aug. 2015. DOI: https://doi.org/10.1016/j.desal.2015.05.009

[16] I. Yılmaz İpek, N. Kabay, M. Bryjak, and M. Yüksel, “Kinetic behaviour of boron selective resins for boron removal using seeded microfiltration system,” React. Funct. Polym., vol. 67, no. 12, pp. 1628–1634, Dec. 2007. DOI: https://doi.org/10.1016/j.reactfunctpolym.2007.07.027

[17] G. R. Krishnan, T. Jayalatha, S. Jacob, R. Rajeev, B. K. George, and B. R. Anjali, “Removal of perchlorate from drinking water using granular activated carbon modified by acidic functional group: Adsorption kinetics and equilibrium studies,” Process Saf. Environ. Prot., vol. 109, pp. 158–171, Jul. 2017. DOI: https://doi.org/10.1016/j.psep.2017.03.014

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Published

20-06-2026

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How to Cite

[1]
Y. SWESI, A. ALHARATI, C. . CHARCOSSET, and K. . FIATY, “Boron Sorption on Selected NMDG Resins: Diffusion Kinetics and Equilibrium Modeling”, JER, vol. 41, no. 2, pp. 1–20, Jun. 2026, doi: 10.66411/jer.v41i2.145.