MaximaLabs

Cobalt from nickel, across one pH unit

A laterite leach liquor contacted counter-currently with D2EHPA in kerosene, then the loaded organic stripped and returned.

20-stage counter-current extraction, solved as a cascadeOperates in the real ~1 pH-unit Co/Ni separation windowExtraction and stripping on one connected flowsheet
Laterite leach liquor
D2EHPA / kerosene
Extraction circuit
Nickel raffinate
Strip acid
Strip circuit
Cobalt strip liquor
Regenerated organic

The actual dark-mode canvas: leach liquor contacted counter-currently with a D2EHPA organic phase that loads cobalt and leaves nickel in the raffinate, then the loaded organic stripped with acid and returned.

A separation that lives on one pH unit

Extraction releases protons, so the distribution coefficient is a steep function of pH — and cobalt's half-extraction pH sits only about one unit below nickel's. The circuit is run in that gap, which is why pH control is the operating variable and why a 20-stage cascade is solved here rather than a single equilibrium contact.

M2+(aq)+2HR(org)MR2(org)+2H+(aq)\mathrm{M^{2+}}_{(aq)} + 2\,\mathrm{HR}_{(org)} \rightleftharpoons \mathrm{MR_2}_{(org)} + 2\,\mathrm{H^+}_{(aq)}
logD=logK+2pH(extraction is a pH-driven ion exchange)\log D = \log K + 2\,\mathrm{pH} \quad \text{(extraction is a pH-driven ion exchange)}
pH50(Co)pH50(Ni)1(the entire basis of the separation)\mathrm{pH}_{50}(\mathrm{Co}) \approx \mathrm{pH}_{50}(\mathrm{Ni}) - 1 \quad \text{(the entire basis of the separation)}

Unit ops shipped for this vertical

Extraction column

Counter-current liquid-liquid contacting — extract and raffinate from a real stage cascade.

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Live plant integration

Stream circuit pH, organic-to-aqueous ratio and raffinate assays from the plant's OPC-UA server into this flowsheet's twin comparison — this separation lives inside a narrow pH band, so a drift of a tenth of a unit is a real cobalt loss.

See the Digital Twin platform →

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