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Process for separating rare-earth element by extraction

A rare earth element and extraction technology, applied in the field of rare earth solvent extraction and separation, can solve the problems of slow and incomplete solid-liquid reaction, affecting product quality, etc., and achieve the effects of eliminating pollution, reducing production costs, and saving three wastes treatment costs

Inactive Publication Date: 2010-07-21
GRIREM ADVANCED MATERIALS CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0009] The above three invention patent applications use alkaline earth metal minerals containing calcium and magnesium, or alkaline earth metal compound powder or slurry containing magnesium and / or calcium, that is, containing magnesium and / or calcium oxides, hydroxides, carbon Salt powder or water slurry is used to pretreat or pre-extract the organic phase. Since alkaline earth metal minerals containing calcium and magnesium and their oxides and hydroxides contain more impurities such as silicon, iron, and aluminum, solid-liquid reaction The speed is slow and incomplete, resulting in three-phase substances in the pretreatment or extraction process, which affects the smooth progress of the extraction process, and impurities such as iron and aluminum are easily extracted into the organic phase, thereby affecting product quality

Method used

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  • Process for separating rare-earth element by extraction
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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] The light-burned magnesia obtained by roasting magnesite at 850-900°C for 2 hours, add 3-5 times of water to digest at 80°C for 30 minutes, then adjust the slurry with water, the liquid-solid weight ratio is 80:1, and pass through Add carbon dioxide gas (concentration: 30%), react at 20°C for 40 minutes, and obtain a pure aqueous solution of magnesium bicarbonate (Mg0: 1.2%) through clarification and filtration.

[0046] Add magnesium bicarbonate aqueous solution at a flow rate of 3.73L / min, lanthanum cerium chloride solution (0.928mol / L) at a flow rate of 0.8L / min, and 1.5mol / L P507 organic phase at a flow rate of 4L / min into the 6-stage pre-extraction Co-flow extraction is carried out in the tank, the mixing time is 25 minutes, and the clarification is 20 minutes to obtain a loaded organic phase containing refractory rare earth ions lanthanum and cerium. The content is less than 0.001mol / L.

[0047] The loaded organic phase is directly used for LaCe / Pr fractional ext...

Embodiment 2

[0049] The mixture of lightly burned magnesia and calcium oxide obtained by roasting dolomite at 800-850°C for 2 hours is digested and mixed with water. The liquid-solid weight ratio is 100:1, and then carbon dioxide gas (concentration is 40%) is introduced. React at 20° C. for 40 minutes, and obtain pure aqueous solution of magnesium bicarbonate and calcium bicarbonate (MgO+CaO: 0.92%) through clarification and filtration.

[0050] Magnesium bicarbonate and calcium bicarbonate aqueous solution are added at a flow rate of 6.4L / min, lanthanum cerium chloride solution (0.665mol / L) is at a flow rate of 1.5L / min, and 1.3mol / L P204 organic phase is added at a flow rate of 6L / min Extraction is carried out in 12-stage pre-extraction tanks, the mixing time is 25 minutes, and after 6-stage co-current and 6-stage countercurrent extraction, a loaded organic phase containing lanthanum and cerium is obtained. The rare earth content REO is 0.165mol / L, and the pH value of the raffinate aqueou...

Embodiment 3

[0053] Calcium oxide obtained by calcining limestone at 800-850°C for 2 hours, digested with water to adjust the slurry, the liquid-solid weight ratio is 16:1, and then pass through carbon dioxide gas (concentration is 60%), react at 70°C for 30 minutes, after After clarification and filtration, a pure aqueous solution of calcium bicarbonate (CaO: 6.25%) was obtained.

[0054] Add the calcium bicarbonate aqueous solution at a flow rate of 1.12L / min, the lanthanum nitrate solution (0.744mol / L) at a flow rate of 1.5L / min, and the 1.5mol / L P507 organic phase at a flow rate of 6L / min into the 8-stage pre-extraction tank Carry out extraction, the mixing time is 25 minutes, after 5 stages of co-current and 3 stages of countercurrent extraction, a loaded organic phase containing refractory rare earth ion lanthanum is obtained, the rare earth content REO is 0.185mol / L, and the pH value of the raffinate aqueous phase is 4.5. REO content 0.0016mol / L.

[0055] The loaded organic phase w...

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Abstract

The invention mixes and pre-extracts the mixed solution of acidic organic extractants such as P507, P204, C272, and naphthenic acid with magnesium bicarbonate and / or calcium bicarbonate solution and rare-earth solution. The rare-earth ions are extracted into the organic phase, then the loaded organic phase containing rare-earth ions are obtained through clarification, and can be used for the extract separation of the mixed rare-earth feed liquid. After a plurality of different levels of extraction, washing, stripping, single rare-earth compounds or rare-earth elements-containing enrichments can be obtained. The magnesium bicarbonate and / or calcium bicarbonate solution are prepared by roasting, digesting, carbonizing magnesite, limestone, calcite, dolomite and similar minerals, so that the content of impurities, such as silicon, iron, aluminum is lower. Ternary phase sediment is not produced in the pre-extraction and extraction separation process, so that the purity of the rare-earth products are not affected. The organic phase does not need ammonia saponification and does not produce ammonia-nitrogen wastewater. By adopting the invention, the production cost of rare-earth products is greatly lowered and the cost for three waste disposal is also greatly saved.

Description

technical field [0001] The invention relates to a process for extracting and separating rare earth elements with an acidic organic extractant. Specifically, the acidic organic extractant is mixed with magnesium bicarbonate and / or calcium bicarbonate aqueous solution and rare earth solution for pre-extraction, and the rare earth ions are extracted into the organic phase, and after clarification, a loaded organic extractant containing rare earth ions is obtained. The invention relates to the extraction and separation of mixed rare earth feed liquid, and belongs to the field of rare earth solvent extraction and separation. Background technique [0002] At present, the separation and purification of a single rare earth element in industry generally adopts solvent extraction. Phosphoric acid), C272 (two (2,4,4-trimethylpentyl) phosphonic acid) and other extractants extract and separate rare earth elements in hydrochloric acid system ([1] Collected Papers on Rare Earth Chemistry,...

Claims

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Application Information

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IPC IPC(8): C22B3/26C22B59/00
CPCY02P10/20
Inventor 黄小卫龙志奇彭新林李红卫杨桂林韩业斌崔大立罗兴华赵娜王良士
Owner GRIREM ADVANCED MATERIALS CO LTD
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