Preparation method for electronic grade high-purity copper sulfate pentahydrate
A technology of copper sulfate pentahydrate, electronic grade, applied in copper sulfate and other directions, can solve the problems of complex process, high price, reducing the activity of plating solution, etc., and achieve the effect of high copper ion concentration, low production cost and high product purity
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Embodiment 1
[0020] (1) Dissolve 500.0 g of industrial-grade copper sulfate pentahydrate to prepare a solution with a copper ion concentration of 35 g / l. At this time, the concentration of each metal impurity in the solution is 0.015 g / l of iron, 0.014 g / l of nickel, and 0.014 g / l of zinc. 0.006g / l, lead 0.0022g / l, use an appropriate amount of sulfuric acid to adjust the pH value of the solution to 1.5, add an appropriate amount of activated carbon to filter;
[0021] (2) Extract copper from the filtrate obtained in step (1) with extractant M5640, the concentration of extractant M5640 in kerosene is 40%, compared to O / A is 2 / 1, the equilibrium pH value is 1.5, and the extraction time is 2min , the number of extraction stages is 4, which separates copper from metal impurities such as iron, nickel, zinc, and lead;
[0022] (3) The extraction agent M5640 in step (2) is loaded with copper organic phase at 55°C for stripping with a stripping agent. The stripping agent is a mixture of sulfuric a...
Embodiment 2
[0025] (1) Dissolve 500.0 g of industrial-grade copper sulfate pentahydrate to prepare a solution with a copper ion concentration of 45 g / l. At this time, the concentration of each metal impurity in the solution is 0.016 g / l of iron, 0.0145 g / l of nickel, and 0.0145 g / l of zinc. 0.0063g / l, lead 0.0025g / l, use an appropriate amount of sulfuric acid to adjust the pH value of the solution to 2.0, add an appropriate amount of activated carbon to filter;
[0026] (2) Extract copper from the filtrate obtained in step (1) with extractant M5640, the concentration of extractant M5640 in kerosene is 45%, compared to O / A is 2 / 1, the equilibrium pH value is 2.0, and the extraction time is 2min , the number of extraction stages is 5, which separates copper from iron, nickel, zinc, lead and other metal impurities;
[0027] (3) Extract the copper-loaded organic phase of extractant M5640 in step (2) at 55°C with a stripping agent for stripping. The stripping agent is a mixture of sulfuric aci...
Embodiment 3
[0030] (1) Dissolve 500.0 g of industrial-grade copper sulfate pentahydrate to prepare a solution with a copper ion concentration of 55 g / l. At this time, the concentration of each metal impurity in the solution is 0.017 g / l of iron, 0.015 g / l of nickel, and 0.0068 g / l of zinc g / l, lead 0.0027g / l, use an appropriate amount of sulfuric acid to adjust the pH value of the solution to 2.5, add an appropriate amount of activated carbon to filter;
[0031] (2) Extract copper from the filtrate obtained in step (1) with extractant M5640, the concentration of extractant M5640 in kerosene is 50%, the ratio O / A is 2 / 1, the equilibrium pH value is 2.5, and the extraction time is 2min , the number of extraction stages is 5, which separates copper from nickel, zinc, iron and other impurities;
[0032] (3) Extract the copper-loaded organic phase of extractant M5640 in step (2) at 55°C with a stripping agent for stripping. The stripping agent is a mixture of sulfuric acid and the mother liquo...
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