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Recovering method for molybdenum and copper in tungsten smelting molybdenum removing slag

A recovery method and molybdenum slag removal technology, applied in the field of tungsten smelting, can solve the problems of complex molybdenum removal slag composition, complicated occurrence conditions, harsh leaching conditions, etc., and achieve the effects of reducing extraction cost, efficient recovery and environmental protection

Active Publication Date: 2015-01-07
CNMC GUANGXI PGMA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, due to the complex composition of molybdenum slag, its main components are Cu, Mo, S, and a small amount of WO 3 Wait
The occurrence of these elements is relatively complicated. According to X-ray diffraction analysis, the occurrence of elements in the molybdenum removal slag is as follows: copper mainly exists in the form of CuS, and Mo mainly exists in the form of MoS 4 2- The compounds formed with Cu exist in the form of compounds, and because the compounds formed by CuS, Cu, Mo, and S are difficult to dissolve in dilute acid and alkali solutions, the existing methods for treating molybdenum slag generally have harsh leaching conditions, and molybdenum, molybdenum, and Low copper leaching rate, incomplete recovery, etc.

Method used

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  • Recovering method for molybdenum and copper in tungsten smelting molybdenum removing slag

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Weigh 100g of molybdenum removal slag, and it has been determined that the main components and contents of molybdenum removal slag are: Mo 16.82%, Cu 28.17%, S 27.43%, WO 3 4.35%; mix the weighed molybdenum removal slag and 3g of quicklime evenly, and then send it into a box-type resistance furnace for roasting. The roasting temperature is 600 ° C. After reaching the roasting temperature, it is kept for 30 minutes; after roasting, it is ball milled to about 400 mesh. The material II was obtained, and the material II was leached with four times the volume of 8% dilute sulfuric acid to obtain a leaching solution, wherein the leaching temperature was 60° C., the leaching time was 1 h, and the stirring speed was 180 r / min.

[0038] The leaching solution was filtered for solid-liquid separation. The contents of molybdenum and copper in the obtained filtrate were 0.07g / mL and 0.12g / mL respectively, and the leaching rates of molybdenum and copper in the molybdenum removal resid...

Embodiment 2

[0040] Weigh 100g of molybdenum removal slag, and it has been determined that the main components and contents of molybdenum removal slag are: Mo 17.65%, Cu29.34%, S 32.84%, WO 3 5.46%; mix the weighed molybdenum removal slag and 3g of quicklime evenly and send it into a box-type resistance furnace for roasting at a roasting temperature of 600°C. After reaching the roasting temperature, keep it warm for 30 minutes; after roasting, carry out ball milling to about 400 mesh. The material II was obtained, and the material II was leached with four times the volume of 8% dilute sulfuric acid to obtain a leaching solution, wherein the leaching temperature was 60° C., the leaching time was 1 h, and the stirring speed was 180 r / min.

[0041] The leaching solution was filtered for solid-liquid separation. The contents of molybdenum and copper in the obtained filtrate were 0.072g / mL and 0.121g / mL respectively, and the leaching rates of molybdenum and copper in the molybdenum removal resid...

Embodiment 3

[0043] Weigh 100g of molybdenum removal slag, and it has been determined that the main components and contents of molybdenum removal slag are: Mo 18.22%, Cu 26.77%, S 27.30%, WO 3 8.14%; mix the weighed molybdenum removal slag and 3g of quicklime evenly and send it to a box-type resistance furnace for roasting at a roasting temperature of 600°C. After reaching the roasting temperature, keep it warm for 30 minutes; The material II was obtained, and the material II was leached with four times the volume of 8% dilute sulfuric acid to obtain a leaching solution, wherein the leaching temperature was 60° C., the leaching time was 1 h, and the stirring speed was 180 r / min.

[0044] The leaching solution was filtered for solid-liquid separation. The contents of molybdenum and copper in the obtained filtrate were 0.074g / mL and 0.11g / mL respectively, and the leaching rates of molybdenum and copper in the molybdenum removal residue reached 98.02% and 97.55%, respectively. The leaching so...

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Abstract

The invention discloses a recovering method for molybdenum and copper in tungsten smelting molybdenum removing slag. The recovering method comprises the following steps: after mixing the molybdenum removing slag and quicklime, feeding the mixture into a resistance furnace for carrying out calcination, ball-milling calcined clinker until a certain granularity is reached, then leaching with dilute sulfuric acid, filtering to obtain filter residues which mainly comprise calcium sulfate and obtain a leaching solution which is an acid solution containing molybdenum and copper, carrying out mixed extraction with a mixed extractant containing N235 and TBP to obtain a water phase which mainly comprises a copper sulfate solution and can be used for a molybdenum removing procedure, reversely extracting an obtained organic phase with ammonia water after washing with dilute sulfuric acid to obtain a water phase which mainly comprises an ammonium molybdate solution, carrying out evaporation crystallization to obtain an ammonium paramolybdate product, wherein the obtained organic phase can be returned to the extraction procedure to be cyclically used. The recovering method has the advantages that the impurity removing effect is great, the product purity is high, the molybdenum and copper yields reach 98% above, obtained side products can also be cyclically utilized, no pollution is generated, the recovering cost is greatly reduced, and the comprehensive economical benefit is improved.

Description

technical field [0001] The invention relates to the technical field of tungsten smelting, in particular to a method for recovering molybdenum and copper from molybdenum slag in tungsten smelting. Background technique [0002] With the development of science and technology, the dependence on non-ferrous metals such as tungsten is increasing. These non-ferrous metal minerals are non-renewable resources with limited reserves. High-grade minerals are becoming less and less, and resources are increasingly scarce. As people pay more and more attention to resource utilization and environmental protection, the rational development and utilization of tungsten resources and the comprehensive recovery of valuable metals from tungsten smelting slag have far-reaching significance, so the comprehensive recycling of tungsten smelting waste slag is imperative. [0003] At present, selective precipitation is mostly used in tungsten smelting to remove molybdenum. The method is: use sodium sul...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/04C22B34/34C22B15/00C22B1/02
CPCY02P10/20
Inventor 班双李敏
Owner CNMC GUANGXI PGMA
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