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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

Inactive Publication Date: 2014-12-10
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since only part of iron, copper and zinc enter the leaching solution in sulfuric acid leaching, most of silver, lead and part of copper and zinc remain in the leaching slag, and rare and precious metals and other valuable elements cannot be recovered.
Moreover, the market for polymerized ferric sulfate products is small, and this process has not achieved industrial production; the second method is to melt and cast iron concentrates from kiln slag into iron anodes, which are treated by electrolysis, and the cathodes produce pure iron products as powder metallurgy Raw material utilization, other valuable elements are recovered from electrolyte or anode slime respectively
This process technology is difficult, coupled with the restrictions on the sales of pure iron products, the economic benefits are difficult to guarantee, and it has not been applied in industry.
[0006] To sum up, the zinc hydrometallurgy kiln slag iron concentrate has a large output and high content of valuable elements, and is a metal resource with high value. Realize comprehensive recycling of resources

Method used

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  • Comprehensive utilization method of slag iron concentrates of wet-type zinc smelting furnace

Examples

Experimental program
Comparison scheme
Effect test

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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Abstract

The invention relates to a comprehensive utilization method of slag iron ore concentrates of a wet-type zinc smelting furnace and belongs to the technical field of metallurgy. The method comprises the following steps: performing two-section counterflow leaching on raw material (slag iron ore concentrates in the wet-type zinc smelting furnace) in the presence of a hydrochloric acid aqueous solution serving as a leaching agent so that valuable metals such as iron, silver, copper, lead, zinc and arsenic in the slag iron ore concentrates enter a leachate; purifying the leachate by utilizing processes of metal iron powder replacement, control over pH (Power Of Hydrogen) value, arsenic sedimentation, sulfuration precipitation and the like, separating the valuable metals such as copper, silver, lead, zinc and arsenic, wherein the purified leachate is a pure FeCl2 aqueous solution; performing thermal decomposition on the pure FeCl2 aqueous solution in a spraying manner so as to obtain Fe2O3 powder; and absorbing the generated HCL gas with water so as to regenerate hydrochloric acid which returns to the leaching process. By the method, the valuable elements in the slag iron ore concentrates of the wet-type zinc smelting furnace are comprehensively separated and recycled; and the hydrochloric acid taken as a leaching agent can be recycled, so that the method realizes resource conservation and is friendly to the environment. During the whole process, the discharge of three wastes is basically avoided; all the resources are utilized to the greatest extent; and obtained products are convenient for subsequent treatment and processing. The method has the advantages of environmental friendliness, economical performance, energy conservation and high resource utilization rate, thereby being convenient for industrial production.

Description

technical field [0001] The invention relates to a method for comprehensive utilization of iron ore slag from a hydrometallurgy zinc kiln, belonging to the technical field of metallurgy. Background technique [0002] In 2011, the output of metal zinc in my country reached 4.46 million tons, of which about 85% were produced by wet method. Zinc hydrometallurgy includes conventional leaching, high temperature and high acid leaching, normal pressure and high pressure oxygen leaching and other processes, all of which have been applied in my country. The output of conventional leaching processes accounts for about 50% of my country's wet zinc production. In the conventional leaching process, the roasted ore is subjected to two-stage countercurrent leaching of neutral and low acid, in which Pb, Au, Ag, In, Ge, Ga, 60% Cu, 30% Cd and 15% Zn enter the leaching residue. The leaching residue is treated by Wiltz method, that is, after drying, it is mixed with 45-55% coke powder, mixed a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B19/00C22B3/10C22B11/00C22B15/00C22B30/04C22B13/00
CPCY02P10/20
Inventor 刘智勇刘志宏李启厚李玉虎何仕超
Owner CENT SOUTH UNIV
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