Method of comprehensively recycling valuable metals from gold concentrate acid leachate
A technology for valuable metals and acid leaching solutions, applied in the direction of non-metallic elements, chemical instruments and methods, sulfur compounds, etc., can solve the problems of waste of zinc and iron resources, high cost of neutralization, land occupation, etc., and achieve zero discharge , reduce treatment costs, and reduce pollution
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Embodiment 1
[0032] A method for comprehensively recovering valuable metals from the acid leaching solution of gold concentrate, comprising the steps of:
[0033] 1) Multi-stage oxidation: introduce the copper-containing acid leaching solution obtained by the roasting and acid leaching process of gold and silver concentrates into three series-connected stirring tanks, add hydrogen peroxide and potassium permanganate to the stirring tanks, and the amount of hydrogen peroxide added is 3kg / m 3 , the amount of potassium permanganate added is 1.0kg / m 3 , the stirring speed is 60r / min, after oxidizing for 3 hours, the oxidized liquid is obtained;
[0034] 2) carbon adsorption of gold and silver: make the oxidized liquid obtained in step 1) flow through the activated carbon adsorption device, and control the flow velocity of the oxidized liquid to be 15m 3 / h, after 4 hours of circulating adsorption, the adsorbed liquid is produced. At this time, gold and silver are effectively adsorbed in the ...
Embodiment 2
[0040] A method for comprehensively recovering valuable metals from the acid leaching solution of gold concentrate, comprising the steps of:
[0041] 1) Multi-stage oxidation: introduce the copper-containing acid leaching solution obtained by the roasting and acid leaching process of gold and silver concentrate into five series-connected stirring tanks, add hydrogen peroxide and potassium permanganate to the stirring tanks, and the amount of hydrogen peroxide added is 5kg / m 3 , the amount of potassium permanganate added is 0.5kg / m 3 , the stirring speed is 50r / min, after oxidation for 5 hours, the oxidized liquid is obtained;
[0042] 2) carbon adsorption of gold and silver: make the oxidized liquid obtained in step 1) flow through the activated carbon adsorption device, and control the flow velocity of the oxidized liquid to be 10m 3 / h, after 5 hours of circulating adsorption, the adsorbed liquid will be produced. At this time, gold and silver are effectively adsorbed in t...
Embodiment 3
[0048] A method for effectively reclaiming zinc from copper-containing acid leaching solution, comprising the steps of:
[0049] 1) Multi-stage oxidation: introduce the copper-containing acid leaching solution obtained by the roasting and acid leaching process of gold and silver concentrates into three series-connected stirring tanks, add hydrogen peroxide and potassium permanganate to the stirring tanks, and the amount of hydrogen peroxide added is 4kg / m 3 , the amount of potassium permanganate added is 0.8kg / m 3 , the stirring speed is 80r / min, after oxidizing for 4 hours, the oxidized liquid is obtained;
[0050] 2) carbon adsorption of gold and silver: make the oxidized liquid obtained in step 1) flow through the activated carbon adsorption device, and control the flow velocity of the oxidized liquid to be 20m 3 / h, after 6 hours of circulating adsorption, the adsorbed liquid is produced. At this time, gold and silver are effectively adsorbed in the activated carbon, and...
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