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From waste to added-value product: A case of efficient separation and recovery of zinc and iron from spent galvanizing acid.

Authors :
Tu, Jiguo
Feng, Xin
Zhang, Bokun
Chen, Libo
Source :
Progress in Natural Science. Aug2024, Vol. 34 Issue 4, p702-709. 8p.
Publication Year :
2024

Abstract

Spent galvanizing acid solution contains high concentrations of zinc salts, ferrous salts, and residual acids, exhibiting extremely high value-added recovery potential. However, achieving the efficient extraction and separation of Zn over Fe becomes particularly challenging under elevated Zn ion concentration. Here, the key extraction parameters, such as modifier ratio, Cyanex 923 concentration and ratio of organic phase to aqueous phase (O/A), are investigated. The stripping and regeneration of extractant, extraction mechanism, as well as high-value recovery of Zn and Fe resources are also comprehensively expounded. After the two-stage extraction, the extraction efficiency of Zn and Fe is 98.92 ​% and 2.09 ​%, respectively. Moreover, the stripping efficiency of Zn reaches 92.3 ​% with O/A ratio of 1 : 2, using oxalic acid as stripping agent. The predominant extracted species is confirmed to be Zn Cl 3 − , resulting in the formation of HZn Cl 3 ∙ R 3 PO complex. More importantly, the regenerated extractant can be recycled back into the extraction process, and the reproduced HCl, high-value recovered ZnO and Fe 2 O 3 can be used for different industrial fields. These findings lay a solid foundation for the efficient separation and comprehensive recovery of high-concentration spent galvanizing acid solution. The developed solvent extraction-stripping-calcination process has achieved the regeneration and recycling of extractant and HCl, as well as efficient recovery of high-value ZnO and Fe 2 O 3. [Display omitted] • Efficient extraction and separation of Zn over Fe from high-concentration spent galvanizing acid have been achieved. • The predominant species Zn Cl 3 − from spent galvanizing acid was extracted in the form of HZn Cl 3 ∙ R 3 PO complex. • Entire solvent extraction-stripping-calcination process realizes recovery of Zn, Fe and HCl, and recycling of extractant. [ABSTRACT FROM AUTHOR]

Details

Language :
English
ISSN :
10020071
Volume :
34
Issue :
4
Database :
Academic Search Index
Journal :
Progress in Natural Science
Publication Type :
Academic Journal
Accession number :
179139790
Full Text :
https://doi.org/10.1016/j.pnsc.2024.06.005