Zinc leaching slag treatment method
A technology of zinc leaching slag and treatment method, applied in the direction of improving process efficiency, can solve the problems of high oxygen concentration and smelting temperature requirements, inability to achieve effective metal enrichment, increase in slag viscosity in side-blown furnaces, etc., to save smelting Cost, beneficial to environmental protection, and the effect of large equipment processing capacity
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Embodiment 1
[0029] A method for treating zinc leaching slag, comprising the steps of:
[0030] 1) Mix the dried zinc leaching slag with 50% coke powder evenly, and then feed it into the volatilization kiln from the feeding chute at the kiln tail. The coke powder is the reducing agent, which will generate carbon monoxide after combustion. The temperature at the kiln tail of the volatilization kiln is 400°C , the kiln tail pressure is -30~50Pa;
[0031] 2) The mixed material produces kiln slag and flue gas under the high temperature condition of 1100 ℃ ~ 1300 ℃ in the volatilization kiln. The lead and zinc in the zinc leaching slag are reduced by carbon monoxide, and the lead and zinc vapor generated is enriched in the flue gas. The flue gas is passed through The surface cooler is cooled to 140-180°C, and then emptied after being purified by the bag filter and desulfurization device. The zinc oxide dust collected at the bottom of the bag filter is transported to the zinc smelting enterprise...
Embodiment 2
[0036] A method for treating zinc leaching slag, comprising the steps of:
[0037] 1) Mix the dried zinc leaching slag with 52% coke powder evenly, and then feed it into the volatilization kiln from the feeding chute at the kiln tail. The coke powder is a reducing agent, which will generate carbon monoxide after combustion. The temperature at the kiln tail of the volatilization kiln is 450°C , the kiln tail pressure is -30~50Pa;
[0038] 2) The mixed material produces kiln slag and flue gas under the high temperature condition of 1100 ℃ ~ 1300 ℃ in the volatilization kiln. The lead and zinc in the zinc leaching slag are reduced by carbon monoxide, and the lead and zinc vapor generated is enriched in the flue gas. The flue gas is passed through The surface cooler is cooled to 140-180°C, and then emptied after being purified by the bag filter and desulfurization device. The zinc oxide dust collected at the bottom of the bag filter is transported to the zinc smelting enterprise t...
Embodiment 3
[0043] A method for treating zinc leaching slag, comprising the steps of:
[0044] 1) Mix the dried zinc leaching slag with 55% coke powder evenly, and then feed it into the volatilization kiln from the feeding chute at the kiln tail, in which the coke powder is the reducing agent and generates carbon monoxide after combustion. The temperature at the kiln tail of the volatilization kiln is 650°C , the kiln tail pressure is -30~50Pa;
[0045] 2) The mixed material produces kiln slag and flue gas under the high temperature condition of 1100 ℃ ~ 1300 ℃ in the volatilization kiln. The lead and zinc in the zinc leaching slag are reduced by carbon monoxide, and the lead and zinc vapor generated is enriched in the flue gas. The flue gas is passed through The surface cooler is cooled to 140-180°C, and then emptied after being purified by the bag filter and desulfurization device. The zinc oxide dust collected at the bottom of the bag filter is transported to the zinc smelting enterpri...
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