Method for producing electrodeposited nickel
An electrowinning and electrowinning cell technology, applied in the field of metallurgy, can solve the problems of large acid fog and poor operating environment in the workshop
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Embodiment 1
[0024] Such as Figure 1-3 The production device shown includes an electrowinning cell body 1, an anode plate 2 and a cathode plate 3 are arranged at intervals in the cell body 1, and a catholyte tube 4 is arranged on one side of the cell body 1, and the catholyte tube 4 extends to the bottom of the cell and Laying along the bottom of the tank from the tank head to the tank end, the catholyte tube 4 is evenly arranged with a number of liquid inlet holes 5, the liquid inlet holes 5 are directly opposite to the cathode plate 3, and the outer layer of the anode plate 2 is provided with a diaphragm bag 6, and the outer layer of the diaphragm bag 6 is An anode cover 7 is provided, the upper part of the anode cover 7 is a sealing cover 701, the lower part is a frame 702, and the upper right side of the sealing cover 701 is provided with a liquid outlet hole 8, the liquid outlet hole 8 is connected to the liquid outlet pipe 9, and the liquid outlet pipe 9 is connected to the anolyte m...
Embodiment 2
[0032] The production device and production process are the same as in Example 1, and the acid mist value measured above the anode area of the electrowinning cell is 0.05 mg / Nm 3 , the average nickel content of the new electrowinning solution is 60.05g / L, the nickel content of the anolyte produced by electrowinning is 37.55g / L, and the nickel electrowinning cycle is 7 days. A total of 6 cycles were investigated, and a total of 6 cycles produced air holes There are 5 boards and 4 grained boards. The average time out of a single electrolytic nickel tank is 12 minutes.
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