Extraction and separation of vanadium from high-acidity stone coal leaching solution using N235 coupling with hydrogen peroxide

• A novel H 2 O 2 –N235 system enabled efficient vanadium extraction from high-acidity leachate by forming peroxovanadates for selective anion exchange.. • Single-stage vanadium extraction efficiency reached 96.99% under optimized conditions, with minimal co-extraction of impurities. • Sulfuric acid–ascorbic acid system effectively stripped vanadium, producing a high-purity vanadium-enriched solution (19.94 g/L). • Mechanistic analysis revealed that vanadium peroxocomplexes were selectively extracted via anion exchange by protonated trialkylamine. • The process was validated at pilot scale, demonstrating industrial feasibility and sustainability. To enhance the efficiency of vanadium extraction and separation from high-acidity stone coal acid leach solution, a novel method based on hydrogen peroxide oxidation and coordination of vanadium ions was proposed in this study. Vanadium was effectively extracted from the high-acidity stone coal leaching solution through a synergistic process involving H₂O₂ oxidation coupled with trialkylamine (N235) extraction. The results indicated that the single-stage vanadium extraction efficiency reached 96.99% under optimal conditions, using 30% N235 (v/v) and 70% sulfonated kerosene as the organic phase, with an initial acidity of 1.5 mol/L, an organic/aqueous phase ratio (O/A) of 2:1, a temperature of 30°C, and an extraction time of 20 min. The V-loaded organic phase was effectively stripped by a mixed solution of sulfuric acid-ascorbic acid. the content of V in the stripping aqueous solution reached up to 19.94g/L, while impurities (Fe, Al, Mn, Si, and Ca) remained below 0.05 g/L. The mechanism of vanadium extraction using the H₂O₂–N235 synergistic system was investigated through slope analysis, saturation extraction experiments, Raman spectroscopy, Fourier transform infrared (FT-IR) spectroscopy, and quantum chemical calculations. Results confirmed that under the oxidation and coordination action of H₂O₂, vanadium ions were converted from VO 2+ cation into stable peroxovanadate anion VO(O 2 )- 2, which were subsequently extracted into the organic phase via an anion-exchange mechanism, forming [VO(O 2 ) 2 (R 3 NH)] complexes. This study addresses the challenges of vanadium extraction from high-acidity stone coal acid leach solution, providing valuable insights for vanadium recovery in industrial applications.

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Publication Details

Journal
Results in Engineering
Published
2025-05-09
DOI
https://doi.org/10.1016/j.rineng.2025.105245
Citations
3
Primary Topic
Metal Extraction and Bioleaching
Type
article
Field-Weighted Citation Impact
2.02

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article

Extraction and separation of vanadium from high-acidity stone coal leaching solution using N235 coupling with hydrogen peroxide

Ou Zhuo, Jun Hua, Feng Gao, Zhaoxia Yang et al.
3 citations
Results in Engineering
Metal Extraction and Bioleaching
2.02
article

Extraction and separation of vanadium from high-acidity stone coal leaching solution using N235 coupling with hydrogen peroxide

Ou Zhuo, Jun Hua, Feng Gao, Zhaoxia Yang, Fei Li, Yimeng Chen, Wenyuan Ma, Hui Zhao, Keyu Shen, Ruixin Luo
article en
3 citations

Abstract

• A novel H 2 O 2 –N235 system enabled efficient vanadium extraction from high-acidity leachate by forming peroxovanadates for selective anion exchange.. • Single-stage vanadium extraction efficiency reached 96.99% under optimized conditions, with minimal co-extraction of impurities. • Sulfuric acid–ascorbic acid system effectively stripped vanadium, producing a high-purity vanadium-enriched solution (19.94 g/L). • Mechanistic analysis revealed that vanadium peroxocomplexes were selectively extracted via anion exchange by protonated trialkylamine. • The process was validated at pilot scale, demonstrating industrial feasibility and sustainability. To enhance the efficiency of vanadium extraction and separation from high-acidity stone coal acid leach solution, a novel method based on hydrogen peroxide oxidation and coordination of vanadium ions was proposed in this study. Vanadium was effectively extracted from the high-acidity stone coal leaching solution through a synergistic process involving H₂O₂ oxidation coupled with trialkylamine (N235) extraction. The results indicated that the single-stage vanadium extraction efficiency reached 96.99% under optimal conditions, using 30% N235 (v/v) and 70% sulfonated kerosene as the organic phase, with an initial acidity of 1.5 mol/L, an organic/aqueous phase ratio (O/A) of 2:1, a temperature of 30°C, and an extraction time of 20 min. The V-loaded organic phase was effectively stripped by a mixed solution of sulfuric acid-ascorbic acid. the content of V in the stripping aqueous solution reached up to 19.94g/L, while impurities (Fe, Al, Mn, Si, and Ca) remained below 0.05 g/L. The mechanism of vanadium extraction using the H₂O₂–N235 synergistic system was investigated through slope analysis, saturation extraction experiments, Raman spectroscopy, Fourier transform infrared (FT-IR) spectroscopy, and quantum chemical calculations. Results confirmed that under the oxidation and coordination action of H₂O₂, vanadium ions were converted from VO 2+ cation into stable peroxovanadate anion VO(O 2 )- 2, which were subsequently extracted into the organic phase via an anion-exchange mechanism, forming [VO(O 2 ) 2 (R 3 NH)] complexes. This study addresses the challenges of vanadium extraction from high-acidity stone coal acid leach solution, providing valuable insights for vanadium recovery in industrial applications.

Results in EngineeringVol. 26
Jishou University (CN)
National Natural Science Foundation of China
Openalex Percentile: Top 14%
Metal Extraction and Bioleaching
2.02
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