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A method for separating and recovering iron from red mud

A technology of separation and recovery and red mud, applied in the field of comprehensive utilization of waste red mud, can solve the problems of slow decomposition rate of ferric oxalate solution in sunlight, large consumption of reagents, pollution, etc., to achieve resource utilization, simple and thorough separation , the effect of reducing environmental pollution

Inactive Publication Date: 2015-11-18
CENT SOUTH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Reduction of red mud by adding carbon after pickling can solve the problem of excessive alkali and iron oxide. However, the reduction process needs to be heated to 1300°C, which consumes a lot of energy and is not economically cost-effective, so it is difficult to apply in industry
The efficiency of leaching iron oxide in red mud with oxalic acid is very high, but the obtained iron oxalate solution has a slow solar decomposition speed, a fast ultraviolet light decomposition speed, and high energy consumption. The loss of oxalic acid during the photolysis process is serious, and the processing cost is high. accept
In addition, red mud is directly leached with oxalic acid solution to remove iron, and about 10% of the oxalic acid is converted into sodium oxalate or sodium hydrogen oxalate and other oxalates remain in the leaching residue, resulting in a large consumption of reagents for the red mud oxalic acid leaching process for iron removal , economically uneconomical
At present, there is no ideal comprehensive method of separating and recycling iron from red mud in the world, and a large amount of red mud can only be stored, causing serious waste of resources and environmental pollution

Method used

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  • A method for separating and recovering iron from red mud
  • A method for separating and recovering iron from red mud
  • A method for separating and recovering iron from red mud

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] Take 100g of red mud, add water to slurry at a solid-liquid ratio of 1:4g / mL, add sulfuric acid to adjust the pH of the solution to 6.5, stir and wash at 50°C for 0.5h, filter, and add the filter cake to 2000ml of oxalic acid with a concentration of 0.5mol / L The solution was stirred and leached at room temperature for 4 hours, and filtered to obtain iron-removing red mud and leaching solution containing iron oxalate. The iron-removed red mud was sampled for testing after drying, and CaO / CaCO was added to the leaching solution containing iron oxalate. 3 The mixture with a molar ratio of 1:6 was adjusted to pH 7.5, stirred at 40 °C for 1 h, and filtered to obtain the mixed filter residue and filtrate of calcium oxalate and ferric hydroxide. The filtrate is returned to prepare red mud leachate, and the filter residue is firstly added with saturated CaCl with a HCl concentration of 2 mol / L at a solid-to-liquid ratio of 1:1 g / ml 2 solution, after slurrying for 0.5h, then sl...

Embodiment 2

[0040] Take 100g of red mud, first add 100ml of sulfuric acid solution with a concentration of 1mol / L, then add 1000ml of oxalic acid solution with a concentration of 1.5mol / L, stir and leaching at 50°C for 2.5h, and filter to obtain iron-removed red mud and leaching solution containing iron oxalate. The iron-removing red mud was sampled and tested after drying. The leaching solution containing iron oxalate was used as the catholyte, and the saturated sulfuric acid-sodium sulfate solution was used as the anolyte. The control cell voltage was 3.7V and the current density was 0.8A / cm. 2 , Membrane electrolysis, ferrous oxalate is precipitated in the catholyte. The ferrous oxalate obtained by filtration was mixed with 6 mol / L hydrochloric acid solution at a solid-liquid ratio of 1:3 g / ml, stirred at 65 °C for 0.5 h, cooled to 5 °C, stirred for 5 h to crystallize out oxalic acid, and filtered to obtain oxalic acid crystals and containing oxalic acid. Ferric chloride solution. The...

Embodiment 3

[0043] Take 100 g of red mud and add 1500 ml of oxalic acid solution with a concentration of 1 mol / L, stir and leaching at 80 °C for 1 hour, and filter to obtain iron-removed red mud and leaching solution containing iron oxalate. The iron-removing red mud was dried and sampled for testing. The leaching solution containing iron oxalate was added with iron powder according to 1.1 times of the chemical reaction amount of Fe(III) reduction to Fe(II), stirred at room temperature for 3 hours, and ferrous oxalate was precipitated, filtered, The ferrous oxalate filter residue and the reduced iron precipitation liquid are obtained. The obtained liquid after reduction and precipitation is returned to prepare red mud leaching solution. The obtained ferrous oxalate filter residue is added with 6 mol / L sulfuric acid solution at a solid-liquid ratio of 1:4 g / ml, stirred at 95 ° C for 0.5 h, and filtered while hot to obtain sulfuric acid. Ferrous filter residue and mixture containing sulfuri...

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Abstract

The invention relates to a method for separating and recovering iron from red mud. The method is characterized by comprising the steps: of leaching out and removing iron from the red mud by using an oxalic acid solution, and filtering to obtain iron-free red mud and an iron oxalate-containing leaching solution, wherein the obtained iron-free red mud can be used as a raw material for producing cement and fireproof bricks; iron oxalate in the obtained leaching solution is reduced to ferrous oxalate through membrane electrolysis or adding a reducing agent and ferrous oxalate is precipitated out, or iron in the solution is separated by directly neutralizing and precipitating an iron hydroxide and oxalate mixture; obtained ferrous oxalate is decomposed to obtain oxalic acid and an iron-containing compound; the obtained iron hydroxide and oxalate mixture is selectively leached out, separated and recovered to obtain oxalic acid and an iron-containing compound; the process of returning recovered oxalic acid to the red mud to leach out and remove iron is cyclically used. The method has the characteristics of short technological process, good iron separation effect, simplicity and convenience in operation, environmental friendliness and the like, and is suitable for large-scale industrialized application.

Description

technical field [0001] The invention belongs to the field of chemical metallurgy, and specifically relates to a method for separating and recovering iron from red mud, which is suitable for comprehensive utilization of waste red mud generated in the alumina production process. Background technique [0002] Red mud is the solid waste produced in the alumina production process. It is red because it contains a large amount of iron oxide, so it is called red mud. Red mud is a residue formed in a high alkalinity sodium aluminate solution. Although it is rinsed with water, it is still alkaline, which brings great difficulties to the storage and utilization of red mud. The output of red mud is about 1 to 1.2 times that of alumina. At present, the annual output of red mud in the world exceeds 50 million tons. The stacking of red mud has become a worldwide problem. [0003] In addition to residual alkali, red mud is mainly aluminum oxide, silicon oxide, calcium oxide, iron oxide, et...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01G49/00
Inventor 王学文杨洋马艺骞王明玉
Owner CENT SOUTH UNIV
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