A method for continuous electrochemical dissolution of ruthenium powder
An electrochemical and ruthenium powder technology is applied in the field of continuous electrochemical dissolution of ruthenium powder, which can solve the problems of difficulty in continuous electrolysis and high-efficiency production.
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Embodiment 1
[0040] (1) Set the electrolytic cell
[0041] according to figure 1 The structure shown sets up the electrolytic cell. The electrolytic cell is made of quartz glass, and the first separator 8 is used to separate the electrolytic cell into five tanks ( figure 1 Only three tanks are shown in the figure, those skilled in the art can understand that according to figure 1 Five tanks are set in the manner shown). The electrode chamber of each cell is 65mm long, 45mm wide and 300mm high. The first partition 8 and the second partition 9 are arranged in parallel, the second partition 9 has a gap of 20 mm from the top, and the bottom has a communication channel 3 with a semicircular cross section. Each cell body is divided into an A electrode chamber and a B electrode chamber by the second separator 9 . The overflow holes 4 (a, b) are opened on the top of the first partition 8 at a distance of 50 mm from the top, and the hole diameter is 10 mm. A hydrochloric acid solution inlet 1...
Embodiment 2
[0046] (1) The arrangement of the electrolytic cell is the same as in Example 1, the difference is that the electrode chamber of each tank body is 65mm long, wide 45mm, and high 320mm; The distance is 70mm.
[0047] (2) The continuous electrolysis of ruthenium powder is the same as embodiment 1, and the difference is that, during the electrolysis reaction, a civilian alternating current of 40 volts is applied at both ends of the A and B electrodes; when the ruthenium content in hydrochloric acid is 31g / L, continue Add hydrochloric acid, control the addition rate of hydrochloric acid to be 15mL / min, this moment be dissolved with the ruthenium-containing hydrochloric acid solution of 31g / L concentration ruthenium to discharge from outlet 2.
Embodiment 3
[0049] (1) The arrangement of the electrolytic cell is the same as in Example 1, the difference is that the electrode chamber of each tank body is 70mm long, wide 40mm, and high 320mm; The distance is 70mm.
[0050] (2) The continuous electrolysis of ruthenium powder is the same as embodiment 1, and the difference is that, during the electrolytic reaction, a civilian alternating current of 60 volts is applied at both ends of the A and B electrodes; when the ruthenium content in hydrochloric acid is 32g / L, continue Add hydrochloric acid, control the addition speed of hydrochloric acid to be 15mL / min, this moment be dissolved with the ruthenium-containing hydrochloric acid solution of 32g / L concentration ruthenium to discharge from outlet 2.
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Abstract
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