DY984N Copper leaching solvent is a un-modified aldoxime-ketoxime reagent. It only can extract copper ions (Cu²⁺) from a pregnant leach solution (PLS) then release (strip) into a highly concentrated sulfuric acid solution, to generate a rich electrolyte suitable for electro-winning (EW).
Article | DY984N |
| Appearance | Amber oil liquid |
| Density (25°C) | 0.907 |
| Flash point | ≥88°C (PMCC) |
| Copper saturation capacity 10% (V/V) | 5.12 g/L Cu |
| Extraction kinetics | ≥92% (30s) |
| Extraction isothermal point | ≥4.4 g/L Cu |
| Phase Stripping time of extraction | ≤57s |
| Stripping kinetics | ≥95% (30s) |
| Stripping isothermal point (Organic) | ≤1.8 g/L Cu |
| Stripping Phase time | ≤43s |
| Copper Net Transfer | 3.4 g/L Cu |
| Cu/Fe selectivity | ≥2500 |
| Liquid phase purity | 98.13 |
The Core Advantages of DY984N copper leaching solvent:
Drop-In Compatibility: DY984N features universal miscibility. It can be added directly to your extraction system without causing phase separation abnormalities, or precipitate clotting.
Radically Reduced Organic Entrainment: It can promote rapid phase disengagement in the settler. Limits both organic and aqueous exchange entrainment, to save the loss of solvent.
Premium Cathode Protection: With a selectivity ratio exceeding 2,500, DY984N prevents ferric iron to contaminat your electrowinning circuit. This maintains maximum current efficiency and get good quality copper cathodes.
Typical Application of DY984N Copper leaching solvent in an extraction cycle:
1. Extraction: Mix the diluted DY984N solvent with the copper-rich PLS (aqueous phase) in a mixer-settler. The extractants selectively bind to copper ions, transferring them into the organic phase.
2. Separation: Settle the mixtur, forming two immiscible phases: the copper-loaded organic phase and the copper-depleted aqueous raffinate.
3. Stripping: The copper-loaded organic phase will be mixed with a strong sulfuric acid solution. The high acidity causes the extractants to release the copper ions into the aqueous phase, creating a rich electrolyte that is high copper content.
4. Electrowinning: The rich electrolyte will be sent to the electrowinning tankhouse, where an electrical current is applied, plating out pure copper (more than 99.995%) onto cathodes.
If you need, please contact us to request a Technical Data Sheet (TDS), Safety Data Sheet (SDS), or a reagent sample kit for laboratory validation testing.
By the way, our metal extractants as below, if you need, please feel free to ask us:
- P204 (D2EHPA or HDEHP) This is used for first step to remove impurity for laterite nickel ore.
- P507 non-ferrous metal extractant for copper, zinc, cobalt-nickel, cadmium, gold-silver, platinum group metals, rare earths and so on.
- DY272 Nickel cobalt separation extractant, it can take cobalt out from nickel cobalt solution, then leave pure nickel.
- DY984N copper solvent extraction reagent.
- QL256-2 Nickel Cobalt Manganese co extraction Extractant.
- DY316 Lithium extractant.
- DY319 high efficiency nickel cobalt co-extraction extractant for battery recycling, can take out nickel and cobalt together from Lithium battery electrolyte.
- DY366 Scandium extractant.
- DY377 efficient nickel and diamond separation extractant.
