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Method for recycling oxalic acid and hydrochloric acid from rare earth oxalate precipitation wastewater

A technology of oxalic acid precipitation and oxalic acid, applied in chemical instruments and methods, separation/purification of carboxylic acid compounds, water pollutants, etc., can solve problems such as increased production costs, unfavorable stripping, and increased difficulty in cleaning precipitation, and achieves reduction The effect of small volume

Active Publication Date: 2017-06-27
NORTHEASTERN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, using a metal salt solution to precipitate and strip oxalic acid will deposit a large amount of precipitate in the extraction tank, which is not conducive to the stripping process, and also increases the difficulty of cleaning the precipitate, thereby increasing the production cost.

Method used

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  • Method for recycling oxalic acid and hydrochloric acid from rare earth oxalate precipitation wastewater

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] In the present embodiment, the method for reclaiming oxalic acid and hydrochloric acid from rare earth oxalic acid precipitation wastewater comprises the following steps:

[0032] 1. Mix N235 with sulfonated kerosene and octanol to obtain an extractant whose volume fraction is 15% of N235, 65% by volume of sulfonated kerosene, and 20% by volume fraction of octanol.

[0033] 2. Mix the rare earth oxalic acid precipitation wastewater with the extractant at a volume ratio of 5:1, the extraction temperature is 25°C, and after 10 stages of extraction, an organic phase loaded with oxalic acid and hydrochloric acid is obtained, and the extraction rates of oxalic acid and hydrochloric acid reach 98%, respectively. 99%.

[0034] 3. Mix the organic phase loaded with oxalic acid and hydrochloric acid and deionized water in a volume ratio of 3:1, and the stripping temperature is 55°C. After 15 stages of stripping, a mixed solution of enriched oxalic acid and hydrochloric acid is ob...

Embodiment 2

[0039] In the present embodiment, the method for reclaiming oxalic acid and hydrochloric acid from rare earth oxalic acid precipitation wastewater comprises the following steps:

[0040] 1. Mix N235 with sulfonated kerosene and octanol to obtain an extractant with a volume fraction of N235 of 20%, a volume fraction of sulfonated kerosene of 65%, and an octanol volume fraction of 15%.

[0041] 2. Mix the rare earth oxalic acid precipitation wastewater with the extractant at a volume ratio of 1:1. The extraction temperature is 35°C. After 12 stages of extraction, an organic phase loaded with oxalic acid and hydrochloric acid is obtained. The extraction rates of oxalic acid and hydrochloric acid reach 98%, respectively. 99%.

[0042] 3. Mix the organic phase loaded with oxalic acid and hydrochloric acid and deionized water in a volume ratio of 5:1, and the stripping temperature is 45°C. After 10 stages of stripping, a mixed solution of enriched oxalic acid and hydrochloric acid is ...

Embodiment 3

[0047] In the present embodiment, the method for reclaiming oxalic acid and hydrochloric acid from rare earth oxalic acid precipitation wastewater comprises the following steps:

[0048] 1. N235 is mixed with sulfonated kerosene and octanol to obtain an extractant with a volume fraction of N235 of 25%, a volume fraction of sulfonated kerosene of 65%, and an octanol volume fraction of 10%.

[0049] 2. Mix the rare earth oxalic acid precipitation wastewater with the extractant at a volume ratio of 0.5︰1. The extraction temperature is 45°C. After 15 stages of extraction, the organic phase loaded with oxalic acid and hydrochloric acid is obtained. The extraction rates of oxalic acid and hydrochloric acid reach 98%, respectively. 99%.

[0050] 3. Mix the organic phase loaded with oxalic acid and hydrochloric acid and deionized water in a volume ratio of 7:1, and the stripping temperature is 35°C. After 8 stages of stripping, a mixed solution of enriched oxalic acid and hydrochloric...

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Abstract

The invention relates to the field of treatment of industrial rare earth wastewater and resource recycling, in particular to a method for recycling oxalic acid and hydrochloric acid from rare earth oxalate precipitation wastewater. The method comprises the following steps: extracting the oxalic acid and the hydrochloric acid from the rare earth oxalate precipitation wastewater through an extraction method, thus obtaining an oxalic acid and hydrochloric acid mixing solution, and recycling the wastewater; and separating the oxalic acid from the hydrochloric acid through the extraction method, thus respectively obtaining an oxalic acid solution and a hydrochloric acid solution. By the use of the method, no rare earth oxalate precipitation wastewater is discharged, and the oxalic acid and the hydrochloric acid are recycled. Valuable resources in the rare earth oxalate precipitation wastewater are recycled, so that the production cost is reduced, and the environmental pollution is relieved.

Description

technical field [0001] The invention relates to the field of rare earth industrial wastewater treatment and resource recycling, in particular to a method for recovering oxalic acid and hydrochloric acid from rare earth oxalic acid precipitation wastewater. Background technique [0002] With the development of science and technology, rare earth oxides, which are the basic materials of high-tech materials, are more and more widely used. Many single oxides are the matrix components of many emerging rare earth functional materials, so they have high purity requirements. Most of the rare earth solutions obtained through extraction, separation and purification are in the form of rare earth chlorides, rare earth sulfates or rare earth nitrates. In order to produce rare earth oxides with higher purity in industry, oxalic acid precipitation is often used to convert them into rare earth oxalate in neutral or weakly acidic solution. In the current rare earth extraction and separation...

Claims

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Application Information

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IPC IPC(8): C02F1/26C01B7/07C07C51/42C07C55/06C02F101/30
CPCC01B7/0737C01P2006/80C02F1/26C02F2101/30C07C51/42C22B59/00C07C55/06
Inventor 边雪李培玉吴文远
Owner NORTHEASTERN UNIV
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