Resource utilization method for Zn, Pb and Ag-containing smelting slag

A technology for recycling smelting slag, which is applied in the field of resource utilization of lead-zinc-silver smelting slag, can solve the problems of unachieved, no resource utilization, and high energy consumption, and achieves short reduction cycle, low recovery cost and simple method. Effect

Active Publication Date: 2017-11-07
白银华鑫九和再生资源有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Traditional fire treatment methods (such as rotary kiln, fuming furnace volatilization treatment, etc.) have high energy consumption and heavy environmental pollution. With the intensification of energy shortage and the improvement of environmental protection requirements, the application of such methods will become less and less
In the wet treatment method, due to the relatively low content of lead and silver in the smelting slag containing lead, zinc and silver, it is still difficult to directly recover lead and silver. In the method, the salts and alum in the slag are not completely decomposed, and the primary leaching rate of zinc and iron is often not high, so the leaching rate of metals still needs to be improved.
The efficient separation of zinc and iron in the leaching solution and the effective utilization of iron resources are major problems faced by wet methods. There are still many deficiencies in current iron removal methods, and the iron-containing slag produced after iron removal is difficult to effectively use. Therefore, wet treatment Methods There are deficiencies in the comprehensive recovery of smelting slag containing lead, zinc and silver. Many methods only recover one or several elements in the smelting slag containing lead, zinc and silver, and the rest will continue to be piled up as waste. To make full use of these resources, but not to achieve substantial emission reduction goals

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] The composition of the lead-zinc-silver smelting slag in this embodiment is: Pb5.6%, Zn8.2%, S12.5%, Ag140g / t, Fe9.8%;

[0025] Put 10kg of the above-mentioned smelting slag with a moisture content of 13% into a drying box for drying, and then into a ball mill for 30 minutes to achieve a particle size of -100 mesh accounting for 78%; and then ball mill coal powder, limestone and industrial soda ash. After ball milling, the particle size reaches -100 mesh, accounting for 76%, 75% and 78%. 9kg of smelting slag containing lead, zinc and silver, 2.1kg of coal powder, 0.9kg of limestone, 0.1kg of industrial soda ash, 0.5kg of bentonite and 1.26kg of water are made into a mixture of ball milled lead, zinc and silver, and then sent to the disc granulator. The granulator rotates at 12r / min to obtain pellets with a diameter of 8-9mm; the pellets are dried at 200°C for 40min and then put into a reduction roaster for 30min at 1200°C to obtain dusty flue gas and roasting Slag; dust-c...

Embodiment 2

[0027] The composition of the lead-zinc-silver smelting slag in this embodiment is: Pb4.8%, Zn7.3%, S15%, Ag128g / t, Fe9.1%;

[0028] Put 10kg of the above-mentioned smelting slag with a water content of 12% into a drying box for drying, and then into a ball mill for 30 minutes to achieve a particle size of -100 mesh accounting for 76%. Then, coal powder, limestone, industrial soda ash, etc. are ball milled respectively, and the particle size after ball milling reaches -100 meshes, accounting for 77%, 75% and 80%. 9kg of smelting slag containing lead, zinc and silver, 2kg of coal powder, 0.8kg of limestone, 0.1kg of industrial soda ash, 0.5kg of bentonite and 1.24kg of water are made into a mixture of ball milled lead, zinc and silver, and then sent to the disc granulator. The speed of the pelletizer is 12r / min, and pellets with a diameter of 9-10mm are obtained; the pellets are dried at 180°C for 45 minutes, and then put into a reduction roaster at 1160°C for 32 minutes to obtain...

Embodiment 3

[0030] The composition of the lead-zinc-silver smelting slag in this embodiment is: Pb6.8%, Zn11.4%, S10.4%, Ag166g / t, Fe11.2%;

[0031] Put 10kg of the above-mentioned smelting slag with 15% moisture content into a drying box for drying, and then into a ball mill for 30 minutes to achieve a particle size of -100 mesh, accounting for 80%. Then, the coal powder, limestone, industrial soda ash, etc. were ball milled, and the particle size after ball milling reached -100 mesh, accounting for 75%, 77%, and 81%. The ball-milled lead-zinc-silver smelting slag 9kg, coal powder 2.25kg, limestone 1.08kg, industrial soda ash 0.27kg, bentonite 0.6kg, water 1.32kg are made into a mixture and then sent to the disc granulator, disc The granulator rotates at 13r / min to obtain pellets with a diameter of 8-10mm. The pellets are dried at 160°C for 50min and then put into a reduction roaster for 35min at 1120°C to obtain dusty flue gas and roasting Dust; dust-containing flue gas passes through the...

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Abstract

The invention discloses a resource utilization method for Zn, Pb and Ag-containing smelting slag, and belongs to the technical field of secondary resource recycling of nonferrous metallurgy. According to the resource utilization method, high-grade PbO and ZnO smoke dust and Ag-enriched roasted slag are obtained by detecting the phase occurrence mode of the Zn, Pb and Ag-containing smelting slag ( containing 3 to 7 percent of Pb, 6 to 12 percent of Zn, 120 to 210 g / t of Ag, 9 to 15 percent of S, 8 to 12 percent of Fe and 12 to 20 percent of SiO2) and changing the states of part valuable metals in the Zn, Pb and Ag-containing smelting slag by utilizing reducing roasting; the smoke dust enters a Pb and Zn smelting system; concentrated Ag ore and tailings are obtained by floating the Ag from the roasted slag; the concentrated Ag ore is directly sold as a product; and the tailings can be externally sold to a cement plant. The overall process does not produce waste slag and wastewater, and is environment-friendly. The method disclosed by the invention is simple in flow; and the direct recovery rates of the Pb, the Zn and the Ag in the smelting slag respectively reach over 98 percent, 95 percent and 96 percent, so that the resource utilization of the valuable metals in the Zn, Pb and Ag-containing smelting slag is realized.

Description

Technical field [0001] The invention belongs to the technical field of secondary resource recovery of non-ferrous metallurgy, in particular to a resource utilization method of lead-zinc-silver smelting slag. Background technique [0002] The smelting slag containing lead, zinc and silver can be smelting slag produced in the process of hydrometallurgical zinc smelting, or it can be process slag containing lead, zinc and silver produced by non-ferrous metal smelting systems such as copper and lead. Under normal circumstances, a hydro-zinc smelting plant with an annual production capacity of 10,000 tons of electro-zinc can produce about 5,000 tons of smelting slag containing lead, zinc and silver each year. my country is a large zinc smelting country, with its zinc output ranking first in the world for many years, and 80% of zinc smelting is hydrometallurgical smelting. Therefore, my country produces a huge amount of lead-zinc-silver smelting slag each year. The long-term stacking ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/04C22B1/243C22B1/02C22B5/10C22B19/00C22B13/02C22B11/00C04B7/147
CPCC04B7/147C22B1/02C22B1/2406C22B1/243C22B5/10C22B7/04C22B11/00C22B13/025C22B19/00Y02P10/20Y02P40/10
Inventor 李俞良于建忠王德海鲁兴武程亮崔海瑞陈一博牛永胜马爱军曹桂银李玉
Owner 白银华鑫九和再生资源有限公司
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