SCI和EI收录∣中国化工学会会刊

中国化学工程学报 ›› 2020, Vol. 28 ›› Issue (4): 1055-1061.DOI: 10.1016/j.cjche.2019.12.003

• Separation Science and Engineering • 上一篇    下一篇

Simple separation method of Zn(II) and Cd(II) from brine solution of zinc plant residue and synthetic chloride media using solvent extraction

Ali Asghar Balesini Aghdam1, Hossein Yoozbashizadeh1, Javad Moghaddam2   

  1. 1 Department of Materials Engineering, Science and Research Branch, Islamic Azad University, Tehran, Iran;
    2 Materials and Metallurgical Engineering Department, University of Zanjan, Zanjan, Iran
  • 收稿日期:2019-09-22 修回日期:2019-11-24 出版日期:2020-04-28 发布日期:2020-07-27
  • 通讯作者: Hossein Yoozbashizadeh
  • 基金资助:
    The authors gratefully acknowledge the Zanjan Zinc Khalessazan Industries Company (ZZKICO), Znajan, Iran and Science and Research Branch, Islamic Azad University (IAU), Tehran, Iran for the financial and technical support of this work.

Simple separation method of Zn(II) and Cd(II) from brine solution of zinc plant residue and synthetic chloride media using solvent extraction

Ali Asghar Balesini Aghdam1, Hossein Yoozbashizadeh1, Javad Moghaddam2   

  1. 1 Department of Materials Engineering, Science and Research Branch, Islamic Azad University, Tehran, Iran;
    2 Materials and Metallurgical Engineering Department, University of Zanjan, Zanjan, Iran
  • Received:2019-09-22 Revised:2019-11-24 Online:2020-04-28 Published:2020-07-27
  • Contact: Hossein Yoozbashizadeh
  • Supported by:
    The authors gratefully acknowledge the Zanjan Zinc Khalessazan Industries Company (ZZKICO), Znajan, Iran and Science and Research Branch, Islamic Azad University (IAU), Tehran, Iran for the financial and technical support of this work.

摘要: In this work, the possibility of separation of Zn2+ and Cd2+ metal ions from chloride (brine) solutions was examined. For this purpose, simple solvent extraction (SX) experiments by di-2-ethylhexyl phosphoric acid (D2EHPA) in kerosene as a diluent was performed on synthetic and industrial chloride solution obtained from brine leaching of zinc filter cakes (by-product of zinc hydrometallurgical processing). The optimal conditions for separation were determined. The zinc extraction efficiency was 99% with negligible co-extraction of cadmium. Therefore, a high ΔpH0.5 value for Zn(Ⅱ) and Cd(Ⅱ) was achieved. FT-IR and slope analysis indicated that ZnClA·3HA and CdClA·3HA species were probably extracted.

关键词: Solvent extraction, Brine media, Leaching filter cakes, Zinc, Cadmium

Abstract: In this work, the possibility of separation of Zn2+ and Cd2+ metal ions from chloride (brine) solutions was examined. For this purpose, simple solvent extraction (SX) experiments by di-2-ethylhexyl phosphoric acid (D2EHPA) in kerosene as a diluent was performed on synthetic and industrial chloride solution obtained from brine leaching of zinc filter cakes (by-product of zinc hydrometallurgical processing). The optimal conditions for separation were determined. The zinc extraction efficiency was 99% with negligible co-extraction of cadmium. Therefore, a high ΔpH0.5 value for Zn(Ⅱ) and Cd(Ⅱ) was achieved. FT-IR and slope analysis indicated that ZnClA·3HA and CdClA·3HA species were probably extracted.

Key words: Solvent extraction, Brine media, Leaching filter cakes, Zinc, Cadmium