Adsorptive removal of lead ions from wastewater using modified diatomite

• The adsorption of Pb(II) ion from water using acid treated diatomite performance was investigated. • The acid treated diatomite (TDE) preparation was investigated at different conditions. • The effects of different adsorption parameters were investigated and optimized. • The adsorption data best fitted the Langmuir and Sips isotherm models. • The adsorption kinetics of Pb(II) on TDE was described by the pseudo second order model. Adsorptive removal techniques offer a promising solution, and this study investigates the synthesis and application of sulfuric acid-modified diatomite for lead ion removal. Modified diatomite synthesized from raw diatomite was chemically modified and the activation parameters (acid concentration (2–10 M), activation time (4–12 h), solid-to-liquid ratio (50–250 g/L), and temperature (50–90 °C)) were optimized to obtain a 77.93 % lead ion removal efficiency under optimal conditions (4 M H₂SO₄, 10 h, 50 g/L, 90 °C). Then, it was characterized using scanning electron microscopy, Fourier transform infrared spectroscopy, Brunauer-Emmett-Teller analysis, and X-ray diffraction. Its structural transformation and surface area increment from 22.39–34.83 m²/g. We evaluated the adsorbent's adsorption efficiency under various experimental conditions, including solution pH (2–10), adsorbent dosage (0.2–1 g/100 mL), contact time (5–75 min), and initial lead ion concentration (10–50 ppm). Adsorption isotherms and kinetics were analyzed using the Langmuir, Freundlich, Sips, and Redlich-Peterson isotherms and pseudo-first-order, pseudo-second-order, and intraparticle diffusion kinetics models. The results demonstrated that modified diatomite effectively removed lead ions from aqueous solutions. Optimal adsorption conditions were determined at pH 7, 0.8 g/100 mL dosage, 45 min contact time, and 10 ppm initial lead ion concentration, yielding a maximum lead removal efficiency of 89.5 %. The adsorption process was well-described by the Langmuir and Sips isotherm models, the best-fit isotherm model, indicating the presence of a monolayer and heterogeneous surface interaction with a maximum adsorption capacity of 25.1 mg/g. Kinetic studies revealed that the intraparticle diffusion kinetics model best fit the kinetic model, suggesting that pore diffusion is the rate-limiting step in the interaction between lead ions and the adsorption site. This study shows that diatomite treated with sulfuric acid has the potential to be a viable and effective adsorbent for the removal of lead ions from wastewater, helping to provide sustainable water treatment solutions.

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Publication Details

Journal
Journal of Hazardous Materials Advances
Published
2025-09-24
DOI
https://doi.org/10.1016/j.hazadv.2025.100900
Citations
1
Primary Topic
Adsorption and biosorption for pollutant removal
Type
article
Field-Weighted Citation Impact
0.82
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article

Adsorptive removal of lead ions from wastewater using modified diatomite

Sintayehu Mekuria Hailegiorgis, Girma Gonfa, Belete Tessema, Sintayehu Shewatatek
1 citations
Journal of Hazardous Materials Advances
Adsorption and biosorption for pollutant removal
0.82
article

Adsorptive removal of lead ions from wastewater using modified diatomite

Sintayehu Mekuria Hailegiorgis, Girma Gonfa, Belete Tessema, Sintayehu Shewatatek
article en
1 citations

Abstract

• The adsorption of Pb(II) ion from water using acid treated diatomite performance was investigated. • The acid treated diatomite (TDE) preparation was investigated at different conditions. • The effects of different adsorption parameters were investigated and optimized. • The adsorption data best fitted the Langmuir and Sips isotherm models. • The adsorption kinetics of Pb(II) on TDE was described by the pseudo second order model. Adsorptive removal techniques offer a promising solution, and this study investigates the synthesis and application of sulfuric acid-modified diatomite for lead ion removal. Modified diatomite synthesized from raw diatomite was chemically modified and the activation parameters (acid concentration (2–10 M), activation time (4–12 h), solid-to-liquid ratio (50–250 g/L), and temperature (50–90 °C)) were optimized to obtain a 77.93 % lead ion removal efficiency under optimal conditions (4 M H₂SO₄, 10 h, 50 g/L, 90 °C). Then, it was characterized using scanning electron microscopy, Fourier transform infrared spectroscopy, Brunauer-Emmett-Teller analysis, and X-ray diffraction. Its structural transformation and surface area increment from 22.39–34.83 m²/g. We evaluated the adsorbent's adsorption efficiency under various experimental conditions, including solution pH (2–10), adsorbent dosage (0.2–1 g/100 mL), contact time (5–75 min), and initial lead ion concentration (10–50 ppm). Adsorption isotherms and kinetics were analyzed using the Langmuir, Freundlich, Sips, and Redlich-Peterson isotherms and pseudo-first-order, pseudo-second-order, and intraparticle diffusion kinetics models. The results demonstrated that modified diatomite effectively removed lead ions from aqueous solutions. Optimal adsorption conditions were determined at pH 7, 0.8 g/100 mL dosage, 45 min contact time, and 10 ppm initial lead ion concentration, yielding a maximum lead removal efficiency of 89.5 %. The adsorption process was well-described by the Langmuir and Sips isotherm models, the best-fit isotherm model, indicating the presence of a monolayer and heterogeneous surface interaction with a maximum adsorption capacity of 25.1 mg/g. Kinetic studies revealed that the intraparticle diffusion kinetics model best fit the kinetic model, suggesting that pore diffusion is the rate-limiting step in the interaction between lead ions and the adsorption site. This study shows that diatomite treated with sulfuric acid has the potential to be a viable and effective adsorbent for the removal of lead ions from wastewater, helping to provide sustainable water treatment solutions.

Journal of Hazardous Materials AdvancesVol. 20
Addis Ababa Science and Technology University (ET)
Openalex Percentile: Top 23%
Adsorption and biosorption for pollutant removal
0.82
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