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Clean metallurgical method for low-temperature molten salt of antimony

A low-temperature molten salt and clean technology, applied in the field of non-ferrous metal metallurgy, can solve the problems of complicated operation, pollute the ecological environment, high production cost, etc., and achieve the effect of reducing antimony smelting temperature, promoting energy saving and emission reduction, and promoting technological progress.

Inactive Publication Date: 2010-12-15
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This process has strong adaptability to raw materials and large processing capacity, but generally has defects such as high coke rate, high energy consumption, huge dust collection system, and complicated operations.
Especially in the blast furnace volatilization smelting process to produce low concentration SO 2 Flue gas, which seriously pollutes the ecological environment, is an unresolved technical problem so far
In order to avoid the disadvantages of environmental pollution in pyrochemical antimony smelting process, alkaline wet antimony smelting process has been used at home and abroad, but it has not been popularized and applied due to high production costs; Due to many problems such as antimony explosion, equipment corrosion, and wastewater treatment, the prospects for industrialization are bleak; the "new chlorination-hydrolysis method" that has been industrialized for more than 20 years can produce high-purity antimony oxide, which is still used by a few manufacturers. However, due to the large amount of wastewater discharge, it is difficult to widely promote

Method used

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  • Clean metallurgical method for low-temperature molten salt of antimony
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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] see figure 1 , the chemical composition of antimony sulfide concentrate is (%): Sb 63.91, Fe 0.94, S 24.91, Cu 0.43, Pb 0.43, Cd 0.0038, As 0.10, SiO 2 5.28 Al 2 o 3 2.38, CaO 1.21, MgO 1.95, the chemical composition of pulverized coal is (%): C 82.33, S 3.01, SiO 2 6.66, CaO 0.83, Al 2 o 3 4.81. Weigh 100g of antimony sulfide concentrate, 9.48g of pulverized coal, 297.02g of industrial grade sodium carbonate and 64.4g of zinc suboxide containing Zn 78.33% and mix evenly. After the mixture is loaded into a graphite crucible, 74.26g of industrial grade sodium carbonate. Push the graphite crucible into a resistance furnace, melt at 900°C for 2 hours, and produce 63.6g of crude antimony containing 99.02% of Sb, and the direct yield of antimony reaches 98.54%; stand at 900°C to clarify and separate the inert molten salt and solid After 1 hour, slowly pour the upper part of the clarified molten salt to obtain 301.5 g of molten sodium carbonate and 155.93 g of soli...

Embodiment 2

[0031] The chemical composition of the antimony sulfide concentrate is the same as in Example 1, and coke powder (containing 82% of C and 10% of ash) is used as a reducing agent. Weigh 100g of antimony sulfide concentrate, 8g of coke and 68.19g of copper oxide calcined sand containing Cu 49.03% and mix evenly. After the mixture is loaded into a graphite crucible, add 301.5g of molten sodium carbonate returned in Example 1, and then cover Example 1. 1 returns NaHCO 392.1g and 22g of technical grade sodium carbonate. Push the graphite crucible into a resistance furnace, melt at 870°C for 3 hours, and produce 64.25g of crude antimony containing 98.78% of Sb, and the direct yield of antimony reaches 99.31%; stand at 800°C to clarify and separate the inert molten salt and solid After 5 hours, slowly pour the upper part of the clarified molten salt to obtain 296.5 g of molten sodium carbonate and 175.43 g of solid slag bonded with a small portion of sodium carbonate. The latter is ...

Embodiment 3

[0033] Using brittle pyrostibite as raw material, its chemical composition is (%): Sb 26.36, Pb 31.33, Zn 3.92, Fe 8.69, Cu 0.12, S 22.10, As 0.58, SiO 2 1.56, CaO 1.44, Al 2 o 3 0.34, coal powder is a reducing agent, and its chemical composition is the same as that of Example 1, and zinc oxide calcine is a sulfur-fixing agent, and its chemical composition is (%): Zn 52.87, Cu 3.58, Pb 0.35, Sb 0.68. Weigh 100g brittle styrofoam concentrate, 80.63g zinc oxide calcine, 10g coal powder, 306g industrial grade sodium bicarbonate and 25.66g industrial grade sodium hydroxide, mix them evenly and put them into a graphite crucible, and then place them in a resistance furnace Melted at 820°C for 4 hours, the output of antimony-lead alloy 56.87g, containing Sb46.58%, Pb 51.42%, the direct yield of antimony and lead were 98.45% and 92.50% respectively; Salt and solid matter, slowly pour the upper part to clarify the molten salt after 3 hours, and obtain 286.25 g of molten sodium carb...

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Abstract

The invention discloses a clean metallurgical method for low-temperature molten salt of antimony, and belongs to the metallurgical field of non-ferrous metals. The method is characterized by comprising the following steps of: performing reductive sulfur-fixing melting on antimony concentrate and oxide of metal with higher sulfur affinity compared with the antimony in low-temperature inert molten salt to generate liquid metal antimony and sulfur-fixed metal sulfide, and forming molten salt slag by using the sulfur-fixed metal sulfide and non-reacted substances as solid substances; and separating most inert molten salt from the solid substances and then thermally returning the most inert molten salt to the melting process, regenerating NaHCO3 for recycling by using the molten salt slag through a 'water leaching-carbonated precipitation' process, reclaiming the sulfur-fixed metal sulfide concentrate for selling from the leached residue by ore dressing, or performing roasting desulfuration on the leached residue for heat energy utilization and smoke acid making, and returning oxide roasting sand serving as a sulfur-fixing agent to the melting process. The method greatly reduces the antimony melting temperature, produces the crude antimony at one step, realizes reclamation of sulfur and energy utilization of sulfide, thoroughly eliminates environmental pollution of low-concentration SO2 smoke at the same time of simplifying the flow, reducing the cost and greatly improving the direct yield of the antimony, and has the advantages of low carbon, cleanness and high efficiency.

Description

technical field [0001] The invention relates to a low-temperature molten salt clean metallurgy method for antimony, which belongs to the field of nonferrous metal metallurgy. Background technique [0002] At present, the smelting process for extracting metal antimony from antimony sulfide concentrate is mainly "blast furnace volatilization smelting-reverberatory furnace reduction smelting". As an alternative process of precipitation smelting, this process first presses or pellets the antimony sulfide concentrate, and then puts it into the blast furnace together with coke and flux. Volatilization and smelting is carried out under the system to volatilize and oxidize antimony sulfide, thereby separating it from gangue and other impurities. The generated antimony oxide and flue gas enter the condensation dust collection system for collection, and then undergo reduction and smelting in a reverberatory furnace to produce crude antimony. This process has strong adaptability to ra...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B30/02
CPCY02P10/20
Inventor 唐谟堂陈永明唐朝波杨建广杨声海何静邵国军
Owner CENT SOUTH UNIV
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