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Method for separating and extracting metallic tungsten and molybdenum from molybdenum removal slag generated by smelting tungsten

A technology for extracting metals and removing molybdenum slag, applied in the direction of improving process efficiency, can solve problems such as unsatisfactory separation effect, high cost, pollution, etc., and achieve the effects of low processing cost, reduced pollution, and simple process

Inactive Publication Date: 2010-07-21
CHENZHOU DIAMOND TUNGSTEN PRODS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the treatment of molybdenum slag is mainly treated by fire roasting to remove sulfur, and the solution of sodium tungstate and sodium molybdate is obtained after alkali dissolution, and the solution with similar tungsten and molybdenum content is used in the subsequent tungsten and molybdenum. The separation process is a bigger problem, the separation effect is not ideal, and the cost is high; and the SO produced by the roasting process 2 serious pollution

Method used

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  • Method for separating and extracting metallic tungsten and molybdenum from molybdenum removal slag generated by smelting tungsten
  • Method for separating and extracting metallic tungsten and molybdenum from molybdenum removal slag generated by smelting tungsten

Examples

Experimental program
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Effect test

Embodiment 1

[0015] Example 1: In the process of removing molybdenum from tungsten smelting, after molybdenum is sulfided into thiomolybdate by a vulcanizing agent, molybdenum removal slag produced by separating molybdenum by selective precipitation method (hereinafter referred to as molybdenum removal slag produced by selective precipitation method), Weigh 200 g as a raw material, and the mass percentage of water (the same in the following embodiments) is 29.3%, tungsten 10.2%, molybdenum 12.8%, and copper 18.3%. Add 1mol / L NaOH solution, heat and stir to dissolve, keep at 60°C, and filter after the pH stabilizes at 11-12 to obtain 135.2g of copper-containing residue, in which moisture is 49.4% and copper is 37.02%. The filtered alkaline solution was neutralized with 2mol / L HCl to a pH of 7.5, neutralized and filtered to obtain 13g of S residue. After neutralization, the solution was cooled to below 60℃, adjusted to pH 2-3 with 2mol / L HCl, then heated to above 90℃, kept for 1 minute and th...

Embodiment 2

[0016] Example 2: Weigh 200 g of the molybdenum removal slag produced by the selective precipitation method, and its moisture content is 29.3%, tungsten 10.2%, molybdenum 12.8%, and copper 18.3%. Add 4mol / L NaOH solution, heat and stir to dissolve, keep at 80°C and keep the pH at 11-12, then filter to obtain 133.9g copper-containing residue, of which moisture is 48.6% and copper is 37.26%. 1mol / L H for dissolving solution 2 SO 4 Neutralize to pH 8.0, neutralize and filter to obtain 10g of S residue. After neutralization, the temperature of the solution is cooled to below 60 ℃, and 1mol / L of H 2 SO 4 Adjust the acid to pH 2-3, then heat to above 90°C, keep it warm for 3 minutes and then cool down. After the temperature is lower than 60°C, filter, filter and wash to obtain 102g of molybdenum trisulfide, of which moisture 46.1%, molybdenum 32.12%, tungsten 0.42%; 1210ml tungsten-containing solution, including tungsten 11.5g / L and molybdenum 0.064g / L. The tungsten-containing solut...

Embodiment 3

[0017] Example 3: In the process of removing molybdenum from tungsten smelting, after molybdenum is sulfided into thiomolybdate by a vulcanizing agent, the molybdenum removal slag (hereinafter referred to as the molybdenum removal slag produced by the acid adjustment method) is separated by the acid precipitation method. Take 100g of dry slag as raw material, of which tungsten is 8.2% and molybdenum is 9.8%. Add 2mol / L NaOH solution, heat and stir to dissolve, keep at 90℃, pH value is stable at 9-10, no residue. 4mol / L H for dissolving solution 2 SO 4 Neutralize to pH 8.5, neutralize and filter to obtain 29g of S residue. After neutralization, the temperature of the solution is cooled to below 60℃, and 4mol / L of H 2 SO 4 Adjust the acid to pH 2-3, then heat to above 90°C, keep it warm for 5 minutes and then cool down, filter, filter and wash after the temperature is below 60°C to obtain 70g of molybdenum trisulfide, of which moisture 45.4%, molybdenum 25.5%, tungsten 0.62%; 15...

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Abstract

The invention provides a novel wet separation method for separating and extracting metallic tungsten and molybdenum from molybdenum-removing slag produced by a sulfide method in the tungsten smelting, sequentially comprising: fully dissolving tungsten and molybdenum metallic elements by directly using (1-4)mol / L alkali solution under the conditions of agitation and temperature of 60 DEG C to 100DEG C to obtain an alkaline solution with a pH value of over 9 and then filter the alkaline solution; neutralizing the solution to have a pH value of 7.5 to 8.5 with (1-4)mol / L acid and filtering the solution; adjusting the acid to make the solution have a pH value of 2 to 3 at a temperature of under 60DEG C, then warming the solution to above 90DEG C and preserving the heat for 1 to 5 minutes, andcooling the solution to under 60DEG C for filtration, so as to obtain an acidulous tungstenic dilute solution and precipitation of molybdenum trisulfide; and gaining a sodium tungstate solution of (100-200)g / L by adopting the conventional process; and the method can effectively separate and extract valuable metals such as tungsten and molybdenum, and has advantages of stable and simple process and low treatment cost.

Description

Technical field [0001] The invention relates to a method for separating and extracting valuable metals such as tungsten and molybdenum from molybdenum removal slag produced by tungsten smelting, in particular to a method for separating and extracting metal tungsten and molybdenum from molybdenum removal slag produced by a sulfidation method in tungsten smelting. Background technique [0002] In the tungsten smelting process, key processes including molybdenum removal are required. The commonly used method for removing molybdenum is to first add a vulcanizing agent to vulcanize, so that molybdenum is preferentially converted into thiomolybdate, and then separate molybdenum through methods such as acid adjustment precipitation and selective precipitation. The molybdenum in the molybdenum removal residue produced by this process is sulfided or sulfur Substituted form exists, and its mass percentage is Mo: 5-15%, which also contains a large amount of tungsten that is entrained or ads...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C22B3/12C22B34/36C22B34/34
CPCY02P10/20
Inventor 曾欣荣梁卫东黄良才胡党
Owner CHENZHOU DIAMOND TUNGSTEN PRODS