Method for reclaiming and purifying platinum and rhodium from waste material containing platinum and rhodium
A technology for platinum and rhodium waste, which is applied in the field of recycling and purifying precious metal platinum and rhodium, can solve problems such as production difficulties, achieve the effects of simple operation, good separation effect, and avoid the loss of rhodium
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Embodiment 1
[0024] The process and steps of this embodiment are as follows:
[0025] (1) Waste material pre-treatment: crushing treatment, according to the mass ratio of metal material: zinc powder = 1:4 ingredients, eutectic at 800 ℃, add aqua regia after cooling, heat and boil until it is completely dissolved, then evaporate the solution with low heat , Then add concentrated HCI to dissolve, and then evaporate to dryness again, three times in succession, until the nitrate is completely removed;
[0026] (2) Removal of base metals: adjust the pH of the solution after the above pretreatment to 1.5-3.5 with 20% NaOH, and flow through the strongly acidic ion exchange resin column at a linear velocity of 0.8 cm / min to remove the base metals in the solution; The base metal resin is darker than the resin without base metal adsorption. Based on this, it can be judged whether the base metal in the solution is cleaned. The base metal-loaded resin is soaked and regenerated with 6MHCI and can be reused...
Embodiment 2
[0036] (1) Waste pretreatment: crushing treatment, metal material: zinc powder = 1:3.6 ingredients, eutectic at 800°C, add aqua regia after cooling, heat and boil until completely dissolved, then evaporate the solution on low heat, and then add Dissolve concentrated HCl, evaporate to dryness again, three consecutive times, until the nitrate is completely eliminated;
[0037] (2) Removal of base metals: adjust the pH of the solution after the above pretreatment to 1.5-3.5 with 20% NaOH, and flow through the strongly acidic ion exchange resin column at a linear velocity of 1.0 cm / min to remove the base metals in the solution; The base metal ion exchange resin is soaked and regenerated with 6MHCI;
[0038] (3) Extraction and separation of platinum and rhodium: Adjust the acidity of the above solution for removing base metals to [H + ]2~5M as the water phase, TBP:260#solvent oil=1:0.5 as the organic phase, three-stage cross-flow extraction to separate platinum at a ratio of 1:1 to sep...
Embodiment 3
[0047] (1) Waste material pre-treatment: crushing treatment, metal material: zinc powder = 1:4.2 ingredients, eutectic at 800°C, add aqua regia after cooling, heat and boil until completely dissolved, then evaporate the solution on low heat, and then add Dissolve concentrated HCl, evaporate to dryness again, three consecutive times, until the nitrate is completely eliminated;
[0048] (2) Removal of base metals: adjust the pH of the solution after the above pretreatment to 2.0-3.5 with 20% NaOH, and flow through the strongly acidic ion exchange resin column at a linear velocity of 0.6 cm / min to remove the base metals in the solution; The base metal ion exchange resin is regenerated by soaking in 6MHCl;
[0049] (3) Extraction and separation of platinum and rhodium: Adjust the acidity of the above solution for removing base metals to [H + ]=3M, and then use the extractant tributyl phosphate to perform three-stage countercurrent extraction and separation of platinum from the solutio...
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