Method for recovering tellurium through cyclone electrolysis of solution containing tellurium
A swirling electrolysis and solution technology, applied in the field of metallurgy, can solve the problems of large influence of cathode tellurium quality and low electrolysis efficiency, and achieve the effects of reducing the concentration of impurity elements, shortening the electrolysis period, and reducing adverse effects
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Embodiment 1
[0030] A method for reclaiming tellurium by swirl electrolysis of a tellurium-containing solution of the present invention comprises the following steps:
[0031] (1) Slowly add sulfuric acid with a concentration of 98% into the tellurium-containing solution. When the pH value of the solution is controlled by a pH meter to 5.7, stop adding concentrated sulfuric acid; Filter to obtain tellurium dioxide precipitate;
[0032] (2) the tellurium dioxide precipitation that step (1) is obtained is that the sodium hydroxide solution leaching (the liquid-solid ratio of sodium hydroxide solution and tellurium dioxide precipitation is 5:1 with the concentration of 100g / L, ratio unit is L / Kg), controlling the leaching temperature to be 90°C, and leaching for 6h to obtain a tellurium leaching solution;
[0033] (3) Add 200g / L tellurium leaching solution to the circulating electrolyzer, adjust the circulating flow rate to 400L / h, and the current density to be 100A / m 2 , to carry out swir...
Embodiment 2
[0036] A method for reclaiming tellurium by swirl electrolysis of a tellurium-containing solution of the present invention comprises the following steps:
[0037] (1) Slowly add sulfuric acid with a concentration of 98% into the tellurium-containing solution. When the pH value of the solution is controlled by a pH meter to 6.0, stop adding concentrated sulfuric acid; Filter to obtain tellurium dioxide precipitate;
[0038] (2) the tellurium dioxide precipitate obtained in step (1) is leached with a concentration of 100g / L of sodium hydroxide solution (the liquid-solid ratio of sodium hydroxide solution and tellurium dioxide precipitate is 6:1, and the ratio unit is L / Kg), controlling the leaching temperature to be 80°C, and leaching for 6h to obtain a tellurium leaching solution;
[0039] (3) Add 100g / L tellurium leaching solution to the circulating electrolyzer, adjust the circulating flow rate to 300L / h, and the current density to 80A / m 2 , to carry out swirl electrolysis...
Embodiment 3
[0042] A method for reclaiming tellurium by swirl electrolysis of a tellurium-containing solution of the present invention comprises the following steps:
[0043](1) Slowly add sulfuric acid with a concentration of 98% into the tellurium-containing solution. When the pH value of the solution is controlled by a pH meter to 6.5, stop adding concentrated sulfuric acid; Filter to obtain tellurium dioxide precipitate;
[0044] (2) the tellurium dioxide precipitate obtained by step (1) is leached with a concentration of sodium hydroxide solution of 120g / L (the liquid-solid ratio of sodium hydroxide solution and tellurium dioxide precipitate is 7:1, and the ratio unit is L / Kg), controlling the leaching temperature to be 60° C., and leaching for 6 hours to obtain a tellurium leaching solution;
[0045] (3) Add 10g / L tellurium leaching solution to the circulating electrolyzer, adjust the circulating flow rate to be 100L / h, and the current density to be 50A / m 2 , carry out swirl elec...
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