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Method for reducing iron and aluminum ions in wet phosphoric acid

A technology for wet-process phosphoric acid and iron in phosphoric acid, applied in chemical instruments and methods, phosphorus compounds, inorganic chemistry, etc., can solve the problems of lack of high-purity phosphoric acid, low impurity removal rate, and large amount of resin, and achieve stable effect. , Simple operation, short process effect

Inactive Publication Date: 2010-12-22
CHINA NAT OFFSHORE OIL CORP +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But all have certain shortcoming, for example: the cost of organic solvent extraction method is higher, and process is complicated; In solvent precipitation method, the separation of phosphoric acid and solvent needs to be distilled, and energy consumption is big (except when back-extracting with alkali), and solvent recovery There is a certain loss, and the removal rate of impurities is not high; the amount of resin used in the ion exchange resin method is large, and it needs to be regenerated; the crystallization method cannot obtain high-purity phosphoric acid in one crystallization, and multiple crystallizations must be carried out. Pure mother liquor is separated, so it is necessary to study the utilization of impure mother liquor, etc.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] A 35% hydrogen peroxide solution with a volume fraction of 0.5% was added to the wet-process phosphoric acid sample for oxidation pretreatment. After 6 hours of reaction, the pretreated wet-process phosphoric acid was obtained. Add 0.5% potassium oxalate and 0.2% sodium carbonate to the pretreated wet-process phosphoric acid at the same time, and react at 25°C for 24h. The iron ion content of the obtained product is 2.15%, and the aluminum ion content is 1.69%. The purification rate of iron ions is 31%, and the purification rate of aluminum ions is 5%.

Embodiment 2

[0021] A 35% hydrogen peroxide solution with a volume fraction of 1% was added to the wet-process phosphoric acid sample for oxidation pretreatment. After 6 hours of reaction, the pretreated wet-process phosphoric acid was obtained. In the pretreated wet-process phosphoric acid, 0.5% potassium oxalate of phosphoric acid mass is first added, and after reaction at 35° C. for 24 hours, 0.2% phosphoric acid mass sodium carbonate is added, and the reaction is continued at 35° C. for 24 hours. The iron ion content of the obtained product is 1.62%, and the aluminum ion content is 1.42%. The purification rate of iron ions is 48%, and the purification rate of aluminum ions is 20%.

Embodiment 3

[0023] A 35% hydrogen peroxide solution with a volume fraction of 1% was added to the wet-process phosphoric acid sample for oxidation pretreatment. After 6 hours of reaction, the pretreated wet-process phosphoric acid was obtained. To the pretreated wet-process phosphoric acid, 0.5% potassium oxalate of phosphoric acid mass was first added, and after 12 hours of reaction at 45°C, 0.2% of phosphoric acid mass sodium carbonate was added, and the reaction was continued at 45°C for 24 hours. The iron ion content in the obtained product is 1.06%, and the aluminum ion content is 1.51%. The purification rate of iron ions is 66%, and the purification rate of aluminum ions is 15%.

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Abstract

The invention discloses a method for reducing iron and aluminum ions in wet phosphoric acid. The method comprises the following steps of: oxidizing wet phosphoric acid with hydrogen peroxide; and adding potassium oxalate and sodium carbonate to the oxidized wet phosphoric acid for carrying out chemical reaction treatment so as to partially removing iron and aluminum ions from the wet phosphoric acid. The method has the advantages of stable effect and simple and convenient operation for removing the iron and aluminum ions from the wet phosphoric acid, and a generated precipitate is not needed to be filtered and can be directly used as an additive for producing a compound fertilizer and added to products without influencing the quality of the compound fertilizer; meanwhile, materials used in the precipitate method has low cost, and can be obtained easily, therefore, the method has stronger competitive force and stronger advantages in industrialized production; and the iron and aluminum ions in the wet phosphoric acid purified by the method are better purified, wherein the purifying rate of iron ions can reach 20-70 percent, and the purifying rate of aluminum ions can reach 5-30 percent.

Description

Technical field [0001] The invention relates to a method for reducing iron and aluminum ions in wet-process phosphoric acid. Background technique [0002] Wet-process phosphoric acid is an intermediate product for the production of ammonium phosphate, heavy superphosphate and a variety of phosphate products. It is an indispensable raw material for metallurgy, petroleum, chemical, electronics, medicine, food and other industries. After preliminary treatment, the wet-process phosphoric acid produced by the factory contains more iron, magnesium, aluminum ions and other impurity ions, which affects the subsequent reaction. Therefore, the current research on the purification method of wet-process phosphoric acid has received extensive attention. Industrial purification methods mainly include crystallization, ion exchange, solvent precipitation, organic solvent extraction, concentration purification, electrodialysis, etc. But they all have certain shortcomings, such as: organic solve...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B25/238
Inventor 王家盛张伟王金铭郑秀兴韩树民
Owner CHINA NAT OFFSHORE OIL CORP
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