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Method for extracting and recovering rare earth elements from waste phosphor

A technology of rare earth elements and fluorescent powder, which is applied in the field of biological extraction, can solve the problems of low recovery rate of rare earth elements, influence on the separation process, and unstable system, and achieve the effect of low cost, simple process and high recovery rate of rare earth elements

Inactive Publication Date: 2014-12-24
龙南市中利再生资源开发有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Supercritical extraction greatly improves the recovery rate and extraction rate of rare earth metals, but the system essentially integrates nitric acid-dissolved phosphor powder with the extraction and separation process, and the uncertainty of the reaction can easily lead to system instability and affect the separation process
Although the above methods have achieved certain research results, there are still problems such as complicated process and low recovery rate of rare earth elements.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0016] A method for extracting and recovering rare earth elements from waste fluorescent powder: Weigh 20g of waste fluorescent powder and add it to a crucible. The chemical composition of the fluorescent powder is: Y 2 o 3 11.57%, CeO 2 1.49%, Tb 4 o 7 0.78%, Eu 2 o 3 1.10%, SiO 2 17.64%, CaO 21.85%, Al 2 o 3 16.08%, P 2 o 5 21.00%, Na 2 O 1.55%, BaO 0.49%, MgO 1.28%, PbO 0.90%, then add 20ml of 98% concentrated sulfuric acid to the crucible, stir evenly, put the crucible in a high-temperature furnace for roasting, the roasting temperature is 400°C, and the roasting time is 2h; take out the roasted solid product, weigh 20g from it and add it to 40ml of water, and carry out leaching reaction under stirring conditions, the reaction temperature is 25°C, and the reaction time is 2h; after the reaction, filter, wash and dry After analyzing the filter residue composition and the filtrate composition, the leaching rate of rare earth is calculated as: Y 2 o 3 82....

Embodiment 2

[0018] A method for extracting and recovering rare earth elements from waste fluorescent powder: Weigh 20g of waste fluorescent powder and add it to a crucible. The chemical composition of the fluorescent powder is: Y 2 o 3 11.57%, CeO 2 1.49%, Tb 4 o 7 0.78%, Eu 2 o 3 1.10%, SiO 2 17.64%, CaO 21.85%, Al 2 o 3 16.08%, P 2 o 5 21.00%, Na 2 O 1.55%, BaO 0.49%, MgO 1.28%, PbO 0.90%, then add 20ml of 98% concentrated sulfuric acid to the crucible, stir evenly, put the crucible in a high-temperature furnace for roasting, the roasting temperature is 300°C, and the roasting time is 2h; take out the roasted solid product, weigh 20g from it and add it to 40ml of water, and carry out the leaching reaction under stirring conditions. The reaction temperature is 25°C, and the reaction time is 2h; after the reaction, filter, wash, and dry After analyzing the filter residue composition and the filtrate composition, the leaching rate of rare earth is calculated as: Y 2 o 3...

Embodiment 3

[0020] A method for extracting and recovering rare earth elements from waste fluorescent powder: Weigh 20g of waste fluorescent powder and add it to a crucible. The chemical composition of the fluorescent powder is: Y 2 o 3 11.57%, CeO 2 1.49%, Tb 4 o 7 0.78%, Eu 2 o 3 1.10%, SiO 2 17.64%, CaO 21.85%, Al 2 o 3 16.08%, P 2 o 5 21.00%, Na 2 O 1.55%, BaO 0.49%, MgO 1.28%, PbO 0.90%, then add 20ml of 98% concentrated sulfuric acid to the crucible, stir evenly, put the crucible in a high temperature furnace for roasting, the roasting temperature is 250°C, and the roasting time is 2h; take out the roasted solid product, weigh 20g from it and add it to 40ml of water, and carry out the leaching reaction under stirring conditions. The reaction temperature is 25°C, and the reaction time is 2h; after the reaction, filter, wash, and dry After analyzing the filter residue composition and the filtrate composition, the leaching rate of rare earth is calculated as: Y 2 o 3...

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Abstract

A method for extracting and recovering rare earth elements from waste phosphor comprises the following steps: (1) concentrated sulfuric acid is added into the waste phosphor, the mixture is uniformly mixed and placed into a high-temperature furnace for roasting, and rare earth is converted into a sulfate form; (2) a solid product after roasting is leached by water, rare earth sulfate enters the water and filtered, a leaching solution after filtering is separated from leaching residues; (3) oxalic acid is added into the leaching solution, pH is adjusted, rare earth is precipitated in a oxalic acid rare earth form, and rare earth oxide is obtained after filtering, drying and roasting. According to the method, the waste phosphor is subjected to processes of sulfatizing roasting, leaching, oxalic acid precipitation, oxalic acid rare earth roasting and the like to recover the rare earth elements in the waste phosphor, the process is simple, the operation is convenient, the cost is lower and the rare earth recovery rate is high.

Description

technical field [0001] The invention relates to the technical field of biological extraction, in particular to a method for extracting and recovering rare earth elements from waste fluorescent powder. Background technique [0002] Rare earth fluorescent lamps have been widely used in lighting systems in most countries at home and abroad due to their advantages of energy saving and environmental protection. At present, the production and usage of rare earth fluorescent lamps in my country ranks first in the world. According to statistics, the annual output of rare earth fluorescent lamps in my country reaches 3.95 billion, and the consumption of trichromatic rare earth phosphors exceeds 5,700 tons. At the same time, more than 400 million rare-earth fluorescent lamps are discarded in my country every year, and the content of rare-earth fluorescent powder is close to 600 tons. At present, most of these discarded fluorescent lamps enter the landfill with domestic waste and are t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B59/00C22B7/00
CPCY02P10/20
Inventor 刘勇赵卓龚跃民
Owner 龙南市中利再生资源开发有限公司
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