Method for recovering valuable metals while leaching zinc from zinc sulfide concentrate with pressurized oxygen
A technology of zinc sulfide concentrate and pressurized oxygen leaching, applied in the direction of improving process efficiency, etc., can solve problems such as low zinc recovery rate, unrealistic, and affecting technical indicators
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Embodiment 1
[0029] The recovery of zinc, heavy metal lead, silver, scattered metal gallium, germanium, indium, etc. in zinc sulfide concentrates with different components is carried out through the following three steps:
[0030] 1) Zinc sulfide concentrate rich in lead, silver and scattered metals produced by a certain factory (element content is Zn50.43%, Pb1.66%, Ag274g / t, Ga204g / t, Ge112g / t, In139g / t) After grinding, the particle size is about 25-40μm, and the solid concentration is about 65%. Pump into the reactor, feed oxygen with a concentration above 98%, and at the same time feed the waste electrolyte after purification and electrowinning to produce zinc. It is leached with high temperature, high pressure and high acid, with a temperature of 145°C, a pressure of 1100kPa, and an acidity of 60g / L. In this way, the sulfur in the zinc sulfide is oxidized to elemental sulfur, and the zinc becomes soluble zinc sulfate. After the leaching pulp is cooled and pressure-reduced in the flas...
Embodiment 2
[0034] 1) Zinc sulfide concentrate rich in lead, silver and scattered metals produced by a certain factory (element content is Zn50.43%, Pb1.66%, Ag274g / t, Ga204g / t, Ge112g / t, In139g / t) After grinding, the particle size is about 25-40μm, and the solid concentration is about 70%. Pump it into the reactor, feed oxygen with a concentration above 98%, and at the same time feed the waste electrolyte after purification and electrowinning to produce zinc, using high temperature, high pressure and high acid leaching, with a temperature of 155°C, a pressure of 1300kPa, and an acidity of 80g / L. After the leached pulp is cooled and pressure-reduced in the flash tank, it is sent to the thickener for separation to obtain the leaching liquid and leaching residue (underflow). The leaching rate of zinc is 98.10%, and the leaching rate of scattered metals is Ga93.10%, Ge91.40%, and In92.20 %, the leaching slag is sent to flotation, the tailings are lead and silver slag, and the lead sending sy...
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