Flash smelting method for lead
A flash smelting and lead sulfide technology, applied in the field of non-ferrous metals, to achieve the effect of reducing the amount of high-temperature flue gas, large production capacity, and efficient utilization of resources
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Embodiment 1
[0021] (1) Spray the powdered lead sulfide concentrate with 8% water content before drying and 0.3% water content after drying with oxygen containing 50% oxygen and 25°C air supply temperature into the space of a high-temperature reaction tower 2 through nozzle 1, forming In the floating state, the input amount of oxygen is controlled so that the oxidation rate of lead sulfide is 60%, the oxidation process of lead sulfide is completed, and the generated melt falls in the sedimentation tank 3 below the reaction tower 2;
[0022] (2) Through the interactive reaction and reduction reaction of lead oxide and lead sulfide, 98% of crude lead and slag are continuously generated; silver is enriched in crude lead, and the recovery rate of silver is 97%;
[0023] (3) crude lead and slag are respectively discharged from the lead outlet 4 and the slag outlet 5 after being clarified and stratified in the sedimentation tank 3, and the slag contains 4% lead and is discarded;
[0024] (4) The...
Embodiment 2
[0026] (1) Spray the powdered lead sulfide concentrate with 8% water content before drying and 0.3% water content after drying with 60% oxygen and 25°C air supply temperature into the space of a high-temperature reaction tower 2 through nozzle 1, forming In the floating state, the input amount of oxygen is controlled, so that the oxidation rate of lead sulfide is 80%, the oxidation process of lead sulfide is completed, and the generated melt falls in the sedimentation tank 3 below the reaction tower 2;
[0027] (2) Through the interactive reaction and reduction reaction of lead oxide and lead sulfide, 97% of crude lead and slag are continuously generated; silver is enriched in crude lead, and the recovery rate of silver is 97.5%;
[0028] (3) crude lead and slag are respectively discharged from the lead outlet 4 and the slag outlet 5 after being clarified and stratified in the sedimentation tank 3, the slag contains 25% lead, and after the slag is reduced by the blast furnace, ...
Embodiment 3
[0031] (1) Spray the powdered lead sulfide concentrate with 8% water content before drying and 0.3% water content after drying with 70% oxygen and 25°C air supply temperature into the space of a high-temperature reaction tower 2 through nozzle 1, forming In the floating state, the input amount of oxygen is controlled so that the oxidation rate of lead sulfide is 70%, the oxidation process of lead sulfide is completed, and the generated melt falls in the sedimentation tank 3 below the reaction tower 2;
[0032] (2) Through the interactive reaction and reduction reaction of lead oxide and lead sulfide, crude lead 97.5% and slag are continuously generated; silver is enriched in crude lead, and the recovery rate of silver is 96%;
[0033] (3) Crude lead and slag are respectively discharged from lead outlet 4 and slag outlet 5 after clarification and stratification in sedimentation tank 3. The slag contains 10% lead and is sent to beneficiation after slow cooling to obtain tailings ...
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