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Method for recycling carbon-ammonia in production process of rare earth oxide

A production process and a technology for oxidizing rare earths, applied in the field of comprehensive utilization of resources

Pending Publication Date: 2021-05-28
GANZHOU NONFERROUS METALLURGICAL RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The method provided by the invention can recycle ammonia and carbon in the preparation process of rare earth oxides, solve the problems of ammonia nitrogen wastewater and greenhouse gas emissions, reduce the cost of ammonium bicarbonate raw materials, and at the same time greatly reduce the ammonia nitrogen content in ammonia nitrogen wastewater , to make it meet emission standards

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  • Method for recycling carbon-ammonia in production process of rare earth oxide
  • Method for recycling carbon-ammonia in production process of rare earth oxide

Examples

Experimental program
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Effect test

Embodiment 1

[0049] The preparation steps of rare earth oxide are:

[0050] (1) Saponification: Saponify the 50vol% P507+50vol% kerosene organic phase with ammonia water to obtain a saponified organic phase;

[0051] (2) Extraction: The saponified organic phase and the rare earth raw material liquid are mixed for extraction and separation, and the rare earth raw material is lanthanum cerium chloride to obtain ammonium chloride-containing wastewater, lanthanum-containing aqueous phase, and cerium-loaded organic phase;

[0052] (3) Stripping: back-extracting the organic phase loaded with cerium with hydrochloric acid to produce a cerium chloride solution.

[0053] (4) Precipitation: adjust the lanthanum chloride concentration of the solution in step (2) at 90g / L, heat up to 65°C, control the concentration of the ammonium bicarbonate solution at 1.5mol / L, add it to the lanthanum chloride solution after preheating , until the pH of the mixed solution is 6.8, let it stand for 2 hours, filter a...

Embodiment 2

[0059] Rare earth raw material is praseodymium neodymium chloride, and the preparation step of rare earth oxide is similar to embodiment 1, and the condition of change is as follows: gained stripping solution is praseodymium neodymium chloride solution, during precipitation, praseodymium neodymium chloride concentration is 70g / L, precipitation temperature is 50°C, and the concentration of ammonium bicarbonate solution is 2mol / L. NdPrO is obtained after drying and calcination of NdPrCO.

[0060] Combine the ammonium chloride wastewater generated during the extraction and precipitation process, adjust the pH value of the ammonium chloride wastewater to 12 using a sodium hydroxide solution with a mass fraction of 32%, preheat it to 70°C, and then enter the ammonia distillation tower to strip and distill ammonia The temperature is 85°C, and the pressure inside the control tower is 0.03MPa. Ammonia vapor is condensed into ammonia water in the tower and discharged from the top of t...

Embodiment 3

[0064] Rare earth raw material is samarium chloride, and the preparation step of rare earth oxide is similar to embodiment 1, and the conditions of change are as follows: stripping liquid is samarium chloride solution, during precipitation, samarium chloride concentration is 100g / L, and precipitation temperature is 25 ℃, The concentration of ammonium bicarbonate solution is 1.2mol / L. Samarium carbonate is dried and calcined to obtain samarium oxide.

[0065] Combine the ammonium chloride wastewater generated during the extraction and precipitation process, adjust the pH value of the ammonium chloride wastewater to 11 using a sodium hydroxide solution with a mass fraction of 32%, preheat it to 70°C, and then enter the ammonia distillation tower to strip and distill ammonia The temperature is 100°C, and the pressure inside the control tower is 0.06MPa. Ammonia vapor is condensed into ammonia water in the tower and discharged from the top of the ammonia distillation tower.

[0...

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Abstract

The invention relates to the technical field of resource comprehensive utilization, and provides a method for recycling carbon-ammonia in a rare earth oxide production process, the rare earth oxide production process comprises the steps of organic phase saponification, extraction, hydrochloric acid reverse extraction, precipitation and calcination, ammonia-nitrogen wastewater is generated in the extraction and precipitation process, carbon dioxide is generated in the precipitation and calcination processes, the ammonia-nitrogen wastewater is subjected to steam stripping ammonia distillation to obtain ammonia water, the obtained ammonia water, water and the carbon dioxide generated in the precipitation and calcination processes are mixed for carbonization to obtain an ammonium bicarbonate solution, and the obtained ammonium bicarbonate solution is returned to the precipitation step to be used as a precipitator. The method provided by the invention can be used to realize treatment of ammonia-nitrogen wastewater, can also reduce the emission of carbon dioxide, reduces the usage amount of ammonium bicarbonate, realizes closed-loop utilization of carbon-ammonia resources, and reduces the preparation cost of rare earth oxide.

Description

technical field [0001] The invention relates to the technical field of comprehensive utilization of resources, in particular to a method for recycling carbon-ammonia in the production process of rare earth oxides. Background technique [0002] Due to their excellent optical, electrical, magnetic and other physical properties, rare earths have played an important role in improving product performance and product structure, and are widely used in defense industry, petrochemical industry, microelectronics industry, new energy, new functional materials and agriculture, etc. multiple fields. [0003] At present, the production process of rare earth oxides in industry is mainly as follows: rare earth raw material mother liquor is extracted and separated-re-extraction to obtain rare earth sulfate or rare earth chloride solution, and then a precipitant is added to prepare rare earth precipitates, and rare earth oxide products are obtained after washing and burning . The rare earth...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01F17/10C01F17/229C01F17/235C01F17/224C01F17/218
CPCC01F17/10C01F17/229C01F17/235C01F17/224C01F17/218
Inventor 郭家旺郭永忠陈冬英赖兰萍周洁英赖耀斌陈后兴王明张积锴伍莺胡小洣
Owner GANZHOU NONFERROUS METALLURGICAL RES INST