Comprehensive utilization method of slag iron concentrates of wet-type zinc smelting furnace
A technology for hydrometallurgy of zinc and iron ore concentrates, applied in the field of metallurgy, can solve problems such as difficult technology, difficult to guarantee economic benefits, failure to realize industrialized production, etc., and achieve the effect of efficient utilization
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Embodiment 1
[0047] The raw material is zinc hydrometallurgy kiln slag iron concentrate. The main components of the raw material are: Fe40%, Ag10g / t, Cu5.0%, Zn5.0%, Pb5.0%, As5.0%, Al 2 o 3 1.0%, S10.0%, SiO 2 6.8%;
[0048] The kiln slag iron concentrate is leached at room temperature, the concentration of hydrochloric acid is 0.5mol / L during low-acid leaching, the liquid-solid ratio is 10:1ml / g, and the leaching time is 240min; 3mol / L hydrochloric acid is carried out high-acid leaching for 180min according to the liquid-solid ratio of 20:1ml / g. The leaching slag obtained by acid leaching is used in the roasting process; after low-acid leaching and high-acid leaching, the leaching rate of Fe in the raw material is 92.21%, the leaching rate of Ag is 98.95%, the leaching rate of copper is 95.07%, and the leaching rate of Pb The leaching rate of As was 99.34%, the leaching rate of As was 88.57%, and the leaching rate of Zn was 57.92%;
[0049] At this moment, the pH value of the low-aci...
Embodiment 2
[0054] The raw material is zinc hydrometallurgy kiln slag iron concentrate. The main components of the raw material are: Fe55.0%, Ag1000g / t, Cu0.5%, Zn5.0%, Pb5.0%, As3.5%, Al 2 o 3 2.0%, S5.0%, SiO 2 4.6%, the rest is oxygen in the oxides of various elements; leaching kiln slag iron concentrate at 60°C, the concentration of hydrochloric acid is 2.5mol / L during low-acid leaching, the liquid-solid ratio is 10:1ml / g, and the leaching time is 180min; the obtained low-acid leaching solution is ready for use, and the obtained low-acid leaching residue is subjected to high-acid leaching for 30 minutes with 5mol / L hydrochloric acid at a liquid-solid ratio of 5:1ml / g. In the low-acid leaching process, the leaching continues according to the low-acid leaching conditions, and the leaching residue obtained from high-acid leaching is used in the roasting process; after low-acid leaching and high-acid leaching, the leaching rate of Fe in the raw material is 91.36%, and the leaching rate o...
Embodiment 3
[0060] Using hydrometallurgy zinc kiln slag iron concentrate as raw material, the composition of the raw material is: Fe56.5%, Ag256g / t, Cu2.5%, Zn2.5%, Pb0.99%, As0.49%, Al 2 o 3 1.8%, S4.75%, SiO 2 3.4%, the rest is oxygen in the oxides of various elements; leaching kiln slag iron concentrate at 90°C, the concentration of hydrochloric acid is 3.0mol / L during low-acid leaching, the liquid-solid ratio is 5:1ml / g, and the leaching time is 30min; The gained low-acid leaching liquid is for subsequent use, and the hydrochloric acid of gained low-acid leaching residue is 5:1ml / g to carry out high-acid leaching 30min with the hydrochloric acid of 6.0mol / L by liquid-solid ratio, after the high-acid leaching, the leachate hydrochloric acid concentration is 3.2mol / L, can Return to the low-acid leaching process, continue leaching according to the low-acid leaching conditions, and use the leaching residue obtained from high-acid leaching for the roasting process; after low-acid leaching...
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