<p>To address the dual challenges of ammonia–nitrogen pollution and high operational costs in conventional rare-earth separation processes, this study has developed a novel P507-unsaponifiable buffered extraction system using maleic acid for sustainable and efficient rare earth recovery. Through systematic optimization of maleic acid concentration (0.2–0.5 mol&#xa0;L<sup>−1</sup>), aqueous phase pH (2.0–3.5), and rare earth loading (0.2–0.5 mol&#xa0;L<sup>−1</sup>), combined with slope method analysis (to determine extraction stoichiometry) and FTIR, the extraction mechanism was clarified. Under optimal conditions (0.5 mol&#xa0;L<sup>−1</sup> maleic acid, 0.5 mol&#xa0;L<sup>−1</sup> rare earth concentration, pH = 3.5), the single-stage extraction capacity of Nd<sup>3+</sup> reached 0.228 mol&#xa0;L<sup>−1</sup>, 75% higher than the traditional P507-kerosene system (0.130 mol&#xa0;L<sup>−1</sup>). Significant improvements were achieved in the separation coefficient for light/medium rare earths (<i>β</i><sub>Sm/Nd</sub> = 12.82), while the heavy rare-earth separation performance remained comparable to conventional systems. Slope analysis and FTIR spectroscopy confirmed that maleic acid acts solely as a buffer without organic-phase coordination. The system completely eliminated ammonia–nitrogen wastewater, reducing treatment costs by 60%, and demonstrated stable performance even at high rare-earth concentrations. This work provides an efficient and industrially scalable solution for green rare-earth separation, aligning with environmental sustainability goals.</p>

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Application of P507-Unsaponifiable Buffer Extraction System in Rare-Earth Separation

  • Huaping Nie,
  • Lei Liu,
  • Tianyu Li,
  • Zhongtang Zhang

摘要

To address the dual challenges of ammonia–nitrogen pollution and high operational costs in conventional rare-earth separation processes, this study has developed a novel P507-unsaponifiable buffered extraction system using maleic acid for sustainable and efficient rare earth recovery. Through systematic optimization of maleic acid concentration (0.2–0.5 mol L−1), aqueous phase pH (2.0–3.5), and rare earth loading (0.2–0.5 mol L−1), combined with slope method analysis (to determine extraction stoichiometry) and FTIR, the extraction mechanism was clarified. Under optimal conditions (0.5 mol L−1 maleic acid, 0.5 mol L−1 rare earth concentration, pH = 3.5), the single-stage extraction capacity of Nd3+ reached 0.228 mol L−1, 75% higher than the traditional P507-kerosene system (0.130 mol L−1). Significant improvements were achieved in the separation coefficient for light/medium rare earths (βSm/Nd = 12.82), while the heavy rare-earth separation performance remained comparable to conventional systems. Slope analysis and FTIR spectroscopy confirmed that maleic acid acts solely as a buffer without organic-phase coordination. The system completely eliminated ammonia–nitrogen wastewater, reducing treatment costs by 60%, and demonstrated stable performance even at high rare-earth concentrations. This work provides an efficient and industrially scalable solution for green rare-earth separation, aligning with environmental sustainability goals.