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
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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.
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