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Method for extracting selenium from nickel-molybdenum ore smelting smoke dust

A technology for nickel-molybdenum ore and soot, applied in the field of extracting selenium from nickel-molybdenum ore smelting soot, can solve the problems of easy leakage of toxic gas, low selenium recovery rate, flying dust, etc. The effect of low selenium and low operating temperature

Inactive Publication Date: 2012-07-11
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In order to eliminate the toxicity of As and Se in nickel-molybdenum ore smelting dust to the environment, recover selenium in dust and realize comprehensive utilization of resources; at the same time, overcome the low selenium recovery rate, high energy consumption and easy production of SO in traditional selenium extraction technology 2 , SeO 2 and As 2 o 3 Toxic gas and other toxic gases are easy to leak, dust to fly, pollute the environment and other disadvantages

Method used

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  • Method for extracting selenium from nickel-molybdenum ore smelting smoke dust
  • Method for extracting selenium from nickel-molybdenum ore smelting smoke dust
  • Method for extracting selenium from nickel-molybdenum ore smelting smoke dust

Examples

Experimental program
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Effect test

Embodiment 1

[0033] Press HCl and H 2 SO 4The molar ratio is 3:2 to prepare 100ml [H + ] is 8mol L -1 leaching agent, turn on the leaching stirring device to make the stirring speed 350r min -1 , set the leaching temperature to 95°C; after reaching the leaching temperature, add 20g of nickel-molybdenum ore smelting dust, and the mass ratio of NaClO 3 / Se=4.5 Add sodium chlorate at a rate of 35mg·min -1 g -1 (Se), leached for 150min; filtered and separated to obtain leachate and leach residue, the composition of which is shown in Table 1.

[0034] Table 1 Main components of leachate and leach residue

[0035] Se

As

Al

Fe

Mo

Ni

Leaching solution (g / L)

7.03

22.03

4.20

5.80

1.98

1.03

Leach residue (%)

0.07

0.41

3.46

2.52

0.07

0.13

[0036] *The volume of leaching solution (including washing solution) is 155ml, and the weight of leaching residue is 6.32g.

[0037...

Embodiment 2

[0042] Press HCl and H 2 SO 4 The molar ratio is 1:2 to prepare 100ml [H + ] is 6mol L -1 leaching agent, turn on the leaching stirring device to make the stirring speed 350r min -1 , set the leaching temperature to 95°C; after reaching the leaching temperature, add 20g of nickel-molybdenum ore smelting dust, and the mass ratio of NaClO 3 / Se=2.0 Add sodium chlorate at a rate of 30mg·min -1 g -1 (Se), leached for 150min; separated by filtration to obtain leachate and leach residue, the components of which are shown in Table 3.

[0043] Table 3 Main components of leachate and leach residue

[0044] Se

As

Al

Fe

Mo

Ni

Leaching solution (g / L)

7.3

23.41

4.12

5.71

2.13

0.98

Leach residue (%)

0.06

0.53

3.63

2.76

0.06

0.15

[0045] * The volume of leaching solution (including washing solution) is 150ml, and the weight of leaching residue is 6.30g.

[0...

Embodiment 3

[0051] Press HCl and H 2 SO 4 The molar ratio is 1:6 to prepare 100ml [H + ] is 5mol L -1 leaching agent, turn on the leaching stirring device to make the stirring speed 350r min -1 , set the leaching temperature to 75°C; after reaching the leaching temperature, add 20g of nickel-molybdenum ore smelting fumes, according to the mass ratio of NaClO 3 / Se=1.0 Add sodium chlorate at a rate of 40mg·min -1 g -1 (Se), leached for 150min; separated by filtration to obtain leachate and leach residue, the composition of which is shown in Table 5.

[0052] Table 5 Main components of leachate and leach residue

[0053] Se

As

Al

Fe

Mo

Ni

Leaching solution (g / L)

6.10

19.48

3.54

5.01

1.86

0.90

Leach residue (%)

0.08

0.71

3.83

2.94

0.12

0.18

[0054] *The volume of leaching liquid (including washing liquid) is 175ml, and the weight of leaching residue is 6.52g. ...

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Abstract

The invention relates to an all-wet smelting process for extracting selenium from nickel-molybdenum ore smelting smoke dust. The process comprises the following steps of: performing oxidation leaching on the nickel-molybdenum ore smelting smoke dust by using sodium chlorate in an HCl-H2SO4 composite system to obtain the selenium to ensure that the selenium in the smoke dust enters leaching liquor; and thoroughly reducing the selenium in the leaching liquor by using sodium sulfite to ensure that high arsenic and high selenium in the leaching liquor can be highly separated, and thus obtaining selenium powder with the purity of 99.68 percent without purification, wherein the recovery rate of all-process selenium is 95.79 percent. The method has the characteristics of short process, low energy consumption, high metal recovery rate and low production cost and is easy to operate, and the aim of clean, energy-saving and environment-friendly metallurgy is fulfilled. More importantly, the method for extracting the selenium from the nickel-molybdenum ore smelting smoke dust is easy to industrialize.

Description

technical field [0001] The invention relates to a selenium hydrometallurgy method, in particular to a method for extracting selenium from nickel-molybdenum ore smelting dust. Background technique [0002] With the rapid development of the modern metallurgical industry, the application fields of nickel and molybdenum continue to expand, resulting in an increase in the demand for nickel and molybdenum year by year. However, there are few independent nickel and molybdenum deposits, and they are gradually exhausted. Nickel-molybdenum ore is a multi-metal composite ore rich in nickel and molybdenum, which is widely distributed in Guizhou, Hunan, Yunnan and Zhejiang in China. Due to its huge reserves and high content of valuable metals nickel and molybdenum (Ni: 0.7%-7.7%, Mo: 2%-11%), it has attracted great attention of metallurgists at home and abroad. According to estimates by Peking University, nickel-molybdenum ore contains 52.2 million tons of molybdenum, 45.15 million ton...

Claims

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Application Information

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IPC IPC(8): C01B19/02
Inventor 侯晓川肖连生高丛堦张启修龚柏藩
Owner CENT SOUTH UNIV