Method for extracting ferric oxide, aluminum oxide and scandium oxide through neutralization of cobaltous hydroxide nickel smelting slag and waste titanium dioxide acid

A technology of cobalt-nickel hydroxide and titanium dioxide waste acid is applied in the direction of improving process efficiency, which can solve the problems of high cost, long process flow, loss of scandium, etc., so as to improve the utilization rate of ore materials, reduce environmental pollution, and reduce the cost. Effect

Active Publication Date: 2017-06-13
万华化学(烟台)电池材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Nickel hydroxide smelting tailings contain a large amount of iron and aluminum. At the same time, during the process of removing iron from nickel hydroxide smelting, a large amount of scandium is also deposited in the iron slag. The existing treatment method is to carry out pyrometallurgical smelting of iron slag into stainless steel ingots for processing, resulting in the loss of scandium
Chinese patent 201510187607.X introduces a method for treating the slag, which uses repeated acid dissolution and repeated precipitation to prepare crude scandium hydroxide. This process has the disadvantages of long process flow, high cost, and ineffective recovery of iron and aluminum.

Method used

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Examples

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Effect test

Embodiment 1

[0028] A method for neutralizing and extracting iron oxide, aluminum oxide and scandium oxide by using cobalt-nickel hydroxide smelting slag and titanium white waste acid, comprising the following steps:

[0029] 1) Mix cobalt-nickel hydroxide smelting slag with titanium white waste acid and water, the weight ratio of the three is 3:1:8, carry out neutralization reaction at 45°C, and control the pH of the reaction end point to 0.5-2.5;

[0030] 2) Add flocculant gelatin to the reaction product of step 1), the amount of gelatin added is 2 / 1000 of the cobalt-nickel hydroxide smelting slag, to precipitate the silicon in the cobalt-nickel hydroxide smelting slag, and then filter the product Obtain filtrate and filter residue;

[0031] 3) Extract the filtrate obtained in step 2) at 60°C. The extraction solvent includes an organic phase and water. The volume ratio of the organic phase to water is 3:1. The number of extraction stages is 8. The organic phase includes an extractant, C...

Embodiment 2

[0038] A method for neutralizing and extracting iron oxide, aluminum oxide and scandium oxide by using cobalt-nickel hydroxide smelting slag and titanium white waste acid, comprising the following steps:

[0039]1) Mix cobalt-nickel hydroxide smelting slag with titanium white waste acid and water, the weight ratio of the three is 3:1:8, carry out neutralization reaction at 65°C, and control the pH of the reaction end point to 0.5-2.5;

[0040] 2) Add flocculant bone glue to the reaction product of step 1), the amount of bone glue added is 5 / 1000 of the mass of the cobalt-nickel hydroxide smelting slag, so as to precipitate the silicon in the cobalt-nickel hydroxide smelting slag, and then the product Filter to obtain filtrate and filter residue;

[0041] 3) Extract the filtrate obtained in step 2) at 40°C, the extraction solvent includes organic phase and water, the volume ratio of the organic phase to water is 5:1, the number of extraction stages is 10, the organic phase incl...

Embodiment 3

[0048] A method for neutralizing and extracting iron oxide, aluminum oxide and scandium oxide by using cobalt-nickel hydroxide smelting slag and titanium white waste acid, comprising the following steps:

[0049] 1) Mix cobalt-nickel hydroxide smelting slag with titanium white waste acid and water, the weight ratio of the three is 3:2:9, carry out neutralization reaction at 85°C, and control the pH of the reaction end point to 0.5-2.5;

[0050] 2) Add flocculant polyacrylamide to the reaction product of step 1), the amount of polyacrylamide added is one-thousandth of the mass of cobalt-nickel hydroxide smelting slag, so as to precipitate the silicon in the cobalt-nickel hydroxide smelting slag , and then filter the product to obtain filtrate and filter residue;

[0051] 3) Extract the filtrate obtained in step 2) at 60°C. The extraction solvent includes an organic phase and water. The volume ratio of the organic phase to water is 3:1. The number of extraction stages is 10. The...

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PUM

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Abstract

The invention relates to a method for extracting ferric oxide, aluminum oxide and scandium oxide through neutralization of cobaltous hydroxide nickel smelting slag and waste titanium dioxide acid. The method comprises the following steps: firstly, performing neutralization on cobaltous hydroxide nickel smelting slag with the waste titanium dioxide acid and water in a certain ratio, adding a flocculant to remove silicon, filtering so as to obtain filtrate, performing reextraction of Al, Fe and Sc in the obtained filtrate by using an extraction agent respectively so as to obtain aluminum salt, ferric salt and Sc(OH)3, performing high-temperature roasting on the ferric salt and the aluminum salt, thereby obtaining oxides with relatively high purity, and roasting the Sc(OH)3, thereby obtaining the scandium oxide. The method has the beneficial effects that valuable metals such as iron and aluminum are extracted by using the cobaltous hydroxide nickel smelting slag, and the rare earth metal scandium is recycled, so that the comprehensive utilization rate of metals in ore can be increased, environment pollution can be reduced, and high economic benefits and environment benefits can be created.

Description

technical field [0001] The invention relates to a method for neutralizing and extracting iron oxide, aluminum oxide and scandium oxide by using cobalt-nickel hydroxide smelting slag and titanium white waste acid, belonging to the field of smelting and leaching of non-ferrous metal ore. Background technique [0002] Titanium dioxide is one of the most important chemical raw materials at home and abroad. At present, there are nearly 100 titanium dioxide factories in my country, with an annual production capacity of 600,000 tons. Except for the production process of Jinzhou titanium dioxide factory, which adopts the chlorination method, the others are all sulfuric acid methods. Production, according to statistics, the production process produces about 8-10 tons of 20% waste acid per ton of titanium dioxide produced, and the waste acid produced every year reaches 4.8-6 million tons. For such a large amount of high-concentration waste acid, domestic titanium dioxide Most white powd...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/04C22B21/00C22B59/00
CPCC22B7/006C22B7/04C22B21/0023C22B59/00Y02P10/20
Inventor 王雪桂张君涛孙杰峰
Owner 万华化学(烟台)电池材料科技有限公司
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