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Process for extracting rare earth from phosphate concentrate

A phosphate concentrate and rare earth technology, which is applied in the extraction of rare earth elements and the whole process technology field, can solve the problems of unsatisfactory extraction and separation of impurity ions and low extraction efficiency, and achieve the goals of saving acid consumption, improving extraction efficiency and reducing impurities The effect of content

Inactive Publication Date: 2012-11-28
贵州黔鸿瑞磷稀土分裂开发有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This process has the following technical defects: (1) The extraction process needs to be acid-adjusted to adjust the pH value to a specified range to obtain a satisfactory extraction rate; (2) In order to improve the extraction effect of rare earths in the neutral extraction system, A large amount of salting-out agent needs to be added; (3) The extraction efficiency is low, and the extraction and separation effect on impurity ions is not ideal

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Rare earth phosphorus concentrate P 2 o 5 36.09%, REO0.14%. Normal temperature hydrochloric acid decomposes once, the solid-to-liquid ratio is 1:3, the decomposition time is 1 hour, and the amount of hydrochloric acid by weight is 0.5 times the weight of ore. Suction filtration is carried out after the decomposition is completed, and the filter residue is washed with warm water at 50-60°C. The rare earth leaching rate is 0.1%, and the primary slag yield is 47%. The amount of nitric acid used for secondary slag decomposition is 0.8 times the ore weight, the solid-liquid ratio is 1:5, the decomposition time is 4.0 hours, and the decomposition temperature is 90°C. Take 400ml P350 and 600ml n-heptane, mix well, and prepare the extracted organic phase. A 100ml separatory funnel was used as a reactor for 8-stage countercurrent extraction, the flow ratio of the organic phase to the solid liquid was 1:2, the extraction mixing time was 5 minutes, and the extraction and clar...

Embodiment 2

[0036] Rare earth phosphorus concentrate P 2 o 5 36.09%, REO0.14%. The primary decomposition temperature of hydrochloric acid is 25°C, the solid-to-liquid ratio is 1:5, and the decomposition time is 3 hours. The amount of hydrochloric acid by weight is 0.8 times the weight of ore. Suction filtration is carried out after the decomposition is completed, and the filter residue is washed with warm water at 50-60°C. The rare earth leaching rate is 3.4%, and the primary slag yield is 32%. The amount of nitric acid used for secondary slag decomposition is 1.2 times the ore weight, the solid-liquid ratio is 1:3, the decomposition time is 2.0 hours, and the decomposition temperature is 60°C. Take 300ml P350 and 700ml n-heptane, mix well, and prepare the extracted organic phase. A 100ml separatory funnel was used as a reactor to carry out 6-stage countercurrent extraction, and the flow ratio of the organic phase to the feed liquid was 1:4. The extraction mixing time is 5min, and t...

Embodiment 3

[0038] Rare earth phosphorus concentrate P 2 o 5 36.09%, REO0.14%. The primary decomposition temperature of hydrochloric acid is 60°C, the solid-to-liquid ratio is 1:2, and the decomposition time is 4 hours. The amount of hydrochloric acid by weight is 1.5 times the weight of ore. Suction filtration is carried out after the decomposition is completed, and the filter residue is washed with warm water at 50-60°C. The rare earth leaching rate is 5.6%, and the primary slag yield is 28%. The amount of nitric acid used for secondary slag decomposition is 1.8 times the ore weight, the solid-liquid ratio is 1:4, the decomposition time is 1.0 hour, and the decomposition temperature is 15°C. Take 700ml P350 and 300ml kerosene, mix well, and prepare the extracted organic phase. A 100ml separatory funnel was used as a reactor to carry out 4-stage countercurrent extraction, and the flow ratio of the organic phase to the feed liquid was 4:1. The extraction mixing time is 5min, and the...

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Abstract

The invention belongs to the field of rare earth metallurgy, and particularly relates to a full-flow process for extracting a rare earth element from rare earth-containing phosphate concentrate. According to the process, phosphate containing 0.05-0.3 percent of REO (Rare Earth Oxide) is used as a raw material, and decomposition is performed once by using low-concentration hydrochloric acid, so that most of impurities in the phosphate concentrate enter solution and the decomposition of the rare earth is effectively suppressed; primary residue is decomposed by using nitric acid, so that valuable metals such as rare earth enter the solution and secondary decomposition solution which meets a subsequent extraction process is prepared; and rare earth extraction is directly performed in a high-acid phosphate secondary decomposition solution system with complex impurity components by using a neutral extraction agent without adding a salting-out agent, and the rare earth is separated in one step under assistance of a washing measure to further separate phosphorus from the rare earth. The purity of the prepared rare earth enrichment is greater than 90 percent and the total rare earth recovery rate is over 90 percent.

Description

technical field [0001] The invention belongs to the field of rare earth metallurgy, and in particular relates to a whole process process for extracting rare earth elements from phosphorus concentrate containing rare earth. Background technique [0002] Many phosphate rocks contain rare earth elements, and rare earth elements are mixed into calcium fluorophosphate or calcium phosphate minerals in the form of isomorphism instead of calcium. Due to the low grade of rare earth, only about 0.1%-0.2% (according to REO), and it exists in mineral phase, it is a worldwide problem to extract rare earth elements from phosphorous concentrate. However, rare earth reserves in phosphate concentrate are large, and the distribution of rare earth elements is good. For example, the distribution of rare earth in Zhijin phosphate rock in Guizhou is medium-yttrium-rich and europium-rich, with reserves reaching 1.8 million tons, which exceeds the weathering crust leaching type in the five province...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C22B59/00C22B3/26
CPCY02P10/20
Inventor 杨幼明聂华平邓庚凤黄龙海谢芳浩邓声华
Owner 贵州黔鸿瑞磷稀土分裂开发有限公司
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