Kinetics and Mechanism of SiO2 Extraction from Acid-Leached Coal Gangue Residue by Alkaline Hydrothermal Treatment

Acid-leached gangue residue is produced after the gangue extraction of metal ions; the main component is silicon, which can be used to extract silica. To ascertain the kinetics and mechanism of silica extraction from acid-leached coal gangue residue, this study explored the effects of the NaOH concentration, solid-to-liquid ratio, reaction temperature, and reaction time on the extraction process. The optimized conditions, determined through this investigation, involved a NaOH concentration of 4 mol/L, a reaction time of 4 h, a solid-to-liquid ratio of 1:4, and a reaction temperature of 180 °C, yielding a SiO<sub>2</sub> extraction ratio of 90.16%. Additionally, the leaching kinetics of silica in a NaOH solution were examined using three kinetic equations from the "unreacted shrinking core model". The results revealed that the control type of the leaching process was the "mixing control", and the apparent activation energy was determined to be 52.36 kJ/mol.

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Publication Details

Journal
Materials
Published
2024-08-23
DOI
https://doi.org/10.3390/ma17174168
Citations
4
Primary Topic
Coal and Its By-products
Type
article
Field-Weighted Citation Impact
1.38
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article

Kinetics and Mechanism of SiO2 Extraction from Acid-Leached Coal Gangue Residue by Alkaline Hydrothermal Treatment

Rongli Jiang, Yuan Gao, Shuojiang Song, Deshun Kong
4 citations
Materials
Coal and Its By-products
1.38
article

Kinetics and Mechanism of SiO2 Extraction from Acid-Leached Coal Gangue Residue by Alkaline Hydrothermal Treatment

Rongli Jiang, Yuan Gao, Shuojiang Song, Deshun Kong
article en
4 citations

Abstract

Acid-leached gangue residue is produced after the gangue extraction of metal ions; the main component is silicon, which can be used to extract silica. To ascertain the kinetics and mechanism of silica extraction from acid-leached coal gangue residue, this study explored the effects of the NaOH concentration, solid-to-liquid ratio, reaction temperature, and reaction time on the extraction process. The optimized conditions, determined through this investigation, involved a NaOH concentration of 4 mol/L, a reaction time of 4 h, a solid-to-liquid ratio of 1:4, and a reaction temperature of 180 °C, yielding a SiO<sub>2</sub> extraction ratio of 90.16%. Additionally, the leaching kinetics of silica in a NaOH solution were examined using three kinetic equations from the "unreacted shrinking core model". The results revealed that the control type of the leaching process was the "mixing control", and the apparent activation energy was determined to be 52.36 kJ/mol.

MaterialsVol. 17(17)
China University of Mining and Technology (CN), Liupanshui Normal University (CN)
Clean water and sanitation
Openalex Percentile: Top 20%
Coal and Its By-products
1.38
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