A continuous low-temperature smelting method for secondary lead
A technology of secondary lead and low temperature, which is applied in the continuous low-temperature smelting of secondary lead and the smelting field of secondary lead, which can solve the problems of increased difficulty, sulfur dioxide pollution, fluctuating sulfur dioxide concentration in flue gas, etc., to reduce smelting energy consumption and low smelting smoke rate , Solve the effect of large fluctuations in sulfur dioxide concentration
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Embodiment 1
[0040] In this example, the lead paste of a certain factory in Anhui was taken as the research object, and 300kg of lead paste (Pb 75.89%, S 6.16%, Si0.62%) was mixed with coal (58.5kg), stones (6kg), iron filings (6kg) , Sodium carbonate (7.5kg) is continuously added to the side-blowing oxidation furnace, and after the addition of the material, it is kept at 1130-1150°C for 3 hours, and the high-lead slag directly flows into the reduction furnace and is kept at 1130-1150°C for 3 hours. Crude lead in the oxidation furnace was 98.33kg (containing 98.78% lead), crude lead in the reduction furnace was 126.51kg (containing 99.12% lead), the total recovery rate of lead was 97.74%, and the smoke and dust rate was 13.88%. Furnace flue gas sulfur dioxide concentration was stable at 0.32%.
Embodiment 2
[0042] The present invention takes the lead paste of a factory in Anhui as the research object, mixes 300kg of lead paste (Pb 75.89%, S 6.16%, Si0.62%) with coal (58.5kg), stones (5kg), iron filings (5kg), Sodium carbonate (9kg) is continuously added into the side-blowing oxidation furnace. After the addition of the material, it is kept at 1120-1140°C for 2.5 hours. The high-lead slag flows directly into the reduction furnace, and it is kept at 1120-1140°C for 2.5 hours. Finally, it is Crude lead in the oxidation furnace was 96.33kg (99.18% lead), crude lead in the reduction furnace was 127.40kg (99.32% lead), the total recovery rate of lead was 97.54%, and the dust rate was 12.16%. The sulfur dioxide concentration in the flue gas of the oxidation furnace was stable at 2.57%. The concentration of sulfur dioxide in furnace flue gas was stable at 0.31%.
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