Low-grade lead-zinc oxide ore smelting system and method
A technology of lead-zinc oxide and a smelting method, applied in the field of mineral metallurgy, can solve the problems of low recovery rate of lead elements, long process flow, unsuitable for low-grade lead-zinc oxide ore, etc., so as to improve the volatilization efficiency of vacuum reduction and improve the extraction efficiency. , the effect of saving energy
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Embodiment 1
[0064] Pre-oxidation reaction: mix the raw ore and quartz sand evenly according to the weight ratio of 100:5, and put them into the pre-oxidation reaction device 10 (rotary kiln). Pass into oxygen-enriched air (O 2 Concentration 35%) for pre-oxidation reaction, the pre-oxidation reaction device 10 (rotary kiln) was heated to 1200 ° C and kept for 2 hours, and naturally cooled to room temperature to obtain kiln slag (pre-oxidation product) and sulfur-containing flue gas. After pre-oxidation treatment, the sulfur content in the kiln slag was reduced from 7.6% to 1.23%. The sulfur-containing flue gas is sequentially processed by the second dust collecting device 50 and the tail gas desulfurization device 40, and the flue gas is discharged after reaching the standard.
[0065] Reduction and volatilization reaction: Mix the kiln slag and coal powder evenly according to the weight ratio of 100:20, and put them into the reduction and volatilization device 21 (vacuum furnace). The v...
Embodiment 2
[0067]Pre-oxidation reaction: mix the raw ore and quartz sand evenly according to the weight ratio of 100:7, and put them into the pre-oxidation reaction device 10 (rotary kiln). Pass into oxygen-enriched air (O 2 concentration of 45%), the pre-oxidation reaction device 10 (rotary kiln) was heated to 1200 ° C and kept for 4 hours, and naturally cooled to room temperature to obtain kiln slag (pre-oxidation product) and sulfur-containing flue gas. After pre-oxidation treatment, the sulfur content in the kiln slag was reduced from 7.6% to 0.98%. The sulfur-containing flue gas is sequentially processed by the second dust collecting device 50 and the tail gas desulfurization device 40, and the flue gas is discharged after reaching the standard.
[0068] Reduction and volatilization reaction: mix the kiln slag and coal powder evenly according to the weight ratio of 100:25, and put them into the reduction and volatilization device 21 (vacuum furnace). The vacuum device 22 (vacuum p...
Embodiment 3
[0070] Pre-oxidation reaction: mix the raw ore and quartz sand evenly according to the weight ratio of 100:7, and put them into the pre-oxidation reaction device 10 (rotary kiln). Air is introduced into the pre-oxidation reaction device 10 (rotary kiln), the temperature of the pre-oxidation reaction device 10 (rotary kiln) is raised to 1100 ° C and kept for 4 hours, and naturally cooled to room temperature to obtain kiln slag (pre-oxidation product) and sulfur-containing fumes gas. After pre-oxidation treatment, the sulfur content in the kiln slag was reduced from 7.6% to 1.98%. The sulfur-containing flue gas is sequentially processed by the second dust collecting device 50 and the tail gas desulfurization device 40, and the flue gas is discharged after reaching the standard.
[0071] Reduction and volatilization reaction: mix the kiln slag and coal powder evenly according to the weight ratio of 100:10, and put them into the reduction and volatilization device 21 (vacuum furn...
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