Energy saving and emission reducing whole wet method zinc smelting technique method
A technology of energy saving, emission reduction and process method, which is applied in the direction of photography process, photography auxiliary process, and process efficiency improvement, etc., can solve the problems of difficulty in processing zinc smelting slag, low recovery rate of associated metals, etc., and saves reagent costs and energy consumption. , the effect of easy industrial production and efficient extraction
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Embodiment 1
[0016] The main composition of the zinc concentrate used is by mass percentage: Zn 36.8%, Pb 10.1%, Cu 7.4%, Cd 0.17%, Co 1.5%, In 0.034%, Ag 1520g / t, of which the particle size is -68um accounting for the zinc concentrate 78%.
[0017] (1) Potential-controlled leaching: the zinc concentrate is slurried at a liquid-solid ratio of 5:1 and then added to the reactor, and chlorine gas is introduced for leaching, and 60L of chlorine gas is injected per ton of ore per hour. The leaching conditions are: concentration of hydrochloric acid The leaching rate is 1mol / L, the leaching temperature is 60°C, and the leaching rates of each metal after 4 hours of reaction are: 98.23%, 98.01%, 97.21%, 95.25%, 96.67%, 97.14%, 97.98%.
[0018] (2) Solution purification: add calcium hydroxide to the solution obtained in step (1) to adjust the pH to 5.0 to remove iron, add zinc powder to the filtered solution, and replace it successively to obtain metal lead, cadmium, copper, cobalt, and silver. Th...
Embodiment 2
[0021] (1) Potential-controlled leaching: the zinc concentrate is mixed according to the liquid-solid ratio of 3:1 and then added to the reactor, and chlorine gas is introduced for leaching, and 80L of chlorine gas is injected per ton of ore per hour. The leaching conditions are: hydrochloric acid The concentration is 1mol / L, the leaching temperature is 50°C, and the leaching rates of each metal after 5 hours of reaction are: 99.01%, 98.56%, 97.23%, 96.36%, 97.09%, 98.76%, 98.12%.
[0022] (2) Solution purification: add calcium oxide to the solution obtained in step (1) to adjust the pH to 4.8 for iron removal, add zinc powder to the solution obtained after filtration, and replace successively to obtain metal lead, cadmium, copper, cobalt, and silver, and the direct yields are respectively 97.21%, 95.65%, 94.37%, 96.19%, 93.14%.
[0023] (3) Closed electrodeposition: the purification solution obtained in step (2) is 390A / m at a current density 2 , the temperature is 37 DEG C ...
Embodiment 3
[0025] (1) Potential-controlled leaching: the zinc concentrate is slurried at a liquid-solid ratio of 6:1 and then added to the reactor, and chlorine gas is introduced to react, and 70L of chlorine gas is injected per ton of ore per hour. The leaching conditions are: concentration of hydrochloric acid The leaching rate is 1mol / L, the leaching temperature is 70°C, and the leaching rates of each metal after 5 hours of reaction are: 98.34%, 97.62%, 98.13%, 96.98%, 97.54%, 97.09%, 97.65%.
[0026] (2) Solution purification: add sodium hydroxide to the solution obtained in step (1) to adjust the pH to 5.0 to remove iron, add zinc powder to the filtered solution, and replace it successively to obtain metal lead, cadmium, copper, cobalt, and silver. They were 97.09%, 96.23%, 93.45%, 96.11%, and 94.23%, respectively.
[0027] (3) Closed electrodeposition: the purification solution obtained in step (2) is 450A / m at a current density 2 , the temperature is 45 DEG C under the condition ...
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