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Recovery method of rare earth elements in ionic rare earth smelting acid dissolution slag

An ionic rare earth and rare earth element technology, applied in the direction of improving process efficiency, can solve the problems of recovering rare earth elements in acid-soluble slag, affecting the recovery effect of rare earth in acid-dissolving slag, etc., to improve efficiency, reduce standards, and improve yield Effect

Active Publication Date: 2013-07-24
NANJING GW ENVIRONMENT ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The rare earth elements precipitated with impurity particles can be dissolved by simple water washing or pickling, but when the impurities are mechanically dehydrated, due to the inherent defects of solid-liquid separation, part of the solution containing rare earth elements remains in the impurities, affecting the acid-dissolved slag. Rare earth recovery effect; rare earth fluorides cannot be dissolved in single ordinary acids such as hydrochloric acid and sulfuric acid, and more oxidizing acids are needed to convert rare earth elements in fluorinated rare earths into soluble rare earth element ions, so simply use a single Common acid can only dissolve a small amount of soluble rare earth elements, and some rare earth fluorides that are difficult to tolerate are still insoluble, and the rare earth elements in the acid-dissolved slag cannot be recovered to the maximum extent.

Method used

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  • Recovery method of rare earth elements in ionic rare earth smelting acid dissolution slag

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Effect test

Embodiment 1

[0024] Add activated acid to the acid-dissolved slag at a mass ratio of 10:1 to 20:1, add water at a mass ratio of 1:2 to 1:5, and perform primary activated water washing. After fully stirring for 1h to 3h, stop stirring and pass through the pump The feed liquid is poured into the plate and frame filter press for primary pressure filtration, and the acid-soluble slag is dehydrated for secondary water washing. The filtrate enters the collection tank and is mixed with oxalic acid wastewater to form oxalic acid rare earth precipitation. After the precipitation process, the oxalic acid rare earth precipitation is pumped The filtrate and the supernatant in the precipitation process are refluxed for primary activation water washing.

[0025] The acid-soluble slag after the first-stage pressure filtration and dehydration is subjected to the second-stage water washing, and the water is added according to the mass ratio of 1:2 to 1:5, and the pH is adjusted to <4 with hydrochloric a...

Embodiment 2

[0028] Acid-soluble slag: The acid-soluble slag produced by the acid-soluble process of an enterprise, the rare earth content, calculated by the total amount of rare earth oxides, namely REO, is 10.3%, the pH is 1.9, and the acid-soluble slag in stock is 2500m 3 , with an annual output of 300m acid-dissolved slag 3 .

[0029] The ratio (mass) of the dosage of activated acid to the acid-dissolved slag is 1:20, and the activated acid is prepared by concentrated hydrochloric acid (1+1) and perchloric acid whose p is 1.67g / ml, and the concentrated hydrochloric acid and perchloric acid The dosing ratio (mass ratio) is 1:4, the ratio (mass ratio) of water dosage to acid-dissolved slag is 2:1, and the washing and stirring time is set to 2h.

[0030] 1t of acid-dissolved slag, in which REO is calculated, the amount of rare earth elements is 0.103t, and 0.05t of activated acid is added according to the mass ratio of 20:1, and 2t of water is added according to the mass ratio of 1...

Embodiment 3

[0035] Acid-soluble slag: The acid-soluble slag produced by the acid-dissolving process of an enterprise, the rare earth content, calculated by the total amount of rare earth oxides, namely REO, is 12.6%, the pH is 2.1, and the acid-soluble slag in stock is 4000m 3 , with an annual output of 300m acid-dissolved slag 3 .

[0036] The ratio (mass) of the dosage of activated acid to the acid-dissolved slag is 1:10, and the activated acid is prepared by the concentrated nitric acid whose p is 1.42g / mL and the perchloric acid whose p is 1.67g / ml. The dosing ratio (mass ratio) of chloric acid is 1:5, the ratio (mass ratio) of water dosage to acid-dissolved slag is 5:1, and the washing and stirring time is set to 3h.

[0037]Add 0.1t of activated acid to 1t of acid-dissolved slag (the amount of rare earth elements is 0.126t in terms of REO) according to the mass ratio of 10:1, and add 5t of water according to the mass ratio of 1:5, perform primary activated water washing, and af...

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Abstract

The invention discloses a recovery method of rare earth elements in ionic rare earth smelting acid dissolution slag for solving technical problems in prior arts. The method comprises the steps of: (1) acid slag primary activation washing; (2) secondary activation washing; (3) ternary activation washing; and (4) rare earth recovery. With the method provided by the invention, rare earth elements in acid dissolution slag can be effectively recovered.

Description

technical field [0001] The invention relates to a method for recovering rare earth elements in acid-dissolved slag formed in the ionic rare earth smelting process, and belongs to the technical field of comprehensive utilization and treatment of solid waste in the rare earth smelting industry. Background technique [0002] Rare earths are widely used in new energy, new materials, energy conservation and environmental protection, aerospace, electronic information and other fields. In the smelting process of ionic rare earths, the first step of acid dissolution process is to dissolve rare earth concentrates with hydrochloric acid to form rich Feed liquid of rare earth elements, some impurities in rare earth concentrate that cannot be dissolved by hydrochloric acid, such as rare earth fluoride, radioactive elements, heavy metal salts, barium salts, gravel, etc., are mechanically dehydrated to form acid-soluble slag. During the formation of acid-dissolved slag, impurity particles...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B7/00C22B3/06C22B3/22C22B3/44C22B59/00
CPCY02P10/20
Inventor 韩正昌韩峰王志磊朱家明张永飞薛超
Owner NANJING GW ENVIRONMENT ENG
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