Projects per year
Abstract
This article outlines an alternative flowsheet for the purification of a multi-metal industrial sidestream (16.3 g/l Ni, 0.7 g/l Co, 0.6 g/l Ca and 1.6 g/l Mg) to allow high-purity nickel recovery. The methodology comprises an initial evaporation step to achieve Ca removal followed by impurity (Ca, Mg) and valuable (Co, Ni) element separation via two-step solvent extraction with organophosphorus extractants. Results indicate that > 80% of Ca is selectively removed as CaSO4 center dot 2H(2)O by evaporation with a concentration degree > 6. In the following treatment, 90% of residual Ca (0.6 g/l) can be selectively extracted with Na-D(2)EHPA. The subsequent solvent extraction step with Na-Cyanex 272 separates Co (> 99%) and Mg (> 95%). The resultant nickel sulfate solution (61.7 g/l Ni, 0.3 g/l Mg and Co 0.007 g/l) of > 99.5% purity can be directly integrated into state-of-the-art nickel recovery processes.
Original language | English |
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Number of pages | 8 |
Journal | JOM |
DOIs | |
Publication status | Published - 4 Dec 2019 |
MoE publication type | A1 Journal article-refereed |
Keywords
- DIRECT SOLVENT-EXTRACTION
- SODIUM-SALTS
- SULFATE
- PURIFICATION
- COBALT
- SEPARATION
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Dive into the research topics of 'High Purity Nickel Recovery from an Industrial Sidestream Using Concentration and Liquid-Liquid Extraction Techniques'. Together they form a unique fingerprint.Projects
- 1 Finished
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BATCIRCLE: Finland-based Circular Ecosystem of Battery Metals
Lundström, M., Porvali, A., Aromaa-Stubb, R., Aromaa, J., Wilson, B., Kalliomäki, T., Karppinen, A., Revitzer, H., Zhang, J., Chernyaev, A., Zou, Y., Hu, F., Ke, P., Liu, F., Rinne, M., Khalid, M. K., Palomäki, H., Partinen, J., Seisko, S., Peng, C., Sahlman, M., Wang, Z., Shukla, S., Forde, G. & Ruismäki, R.
01/01/2019 → 30/04/2021
Project: Business Finland: Other research funding
Equipment
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Raw Materials Research Infrastructure
Maarit Karppinen (Manager)
School of Chemical EngineeringFacility/equipment: Facility