Abstract
Solvent extraction is an effective method for addressing the difficult separation of Cr3+ and Fe3+ in sulfuric acid media. Bis(2-ethylhexyl)phosphate (P204) has been shown to extract Fe3+ from systems where Cr3+ and Fe3+ coexist. However, the issue of co-extraction of chromium remains. Considering that 2-ethylhexyl 2-ethylhexylphosphate (P507) and P204 are the same class of extractants, this study proposes the use of P507 to separate Cr3+ and Fe3+. Under optimal conditions, the primary extraction efficiency for Fe3+ reached 99.65%, with Cr3+ being co-extracted at only 5.93%, and Al being co-extracted by 8.66%. The co-extracted Al3+ was removed by a three-stage cross-current scrubbing process. After three-stage counter-current stripping, selective stripping of iron was achieved, leading to the effective separation of Cr3+ and Fe3+. To date, no studies have reported on the role of sulfate ions in the extraction of Fe3+ by P507. This study for the first time, reveals a new extraction mechanism in which sulfate ions (SO42−) play a role in the formation of complexes during the extraction process. It also provides a technological foundation for the further recovery of high-purity Cr3+ and offers valuable insights into the behavior of sulfate ions during the extraction process.
| Original language | English |
|---|---|
| Article number | 165481 |
| Journal | Chemical Engineering Journal |
| Volume | 519 |
| DOIs | |
| State | Published - 1 Sep 2025 |
| Externally published | Yes |
Keywords
- Chromium sludge
- Cr
- Fe
- Separation
- Solvent extraction
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