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Method for comprehensively recycling rare earth and fluorine in process of treating bastnaesite

A bastnaesite and treatment process technology, applied in the field of rare earth hydrometallurgy, can solve the problems of increasing environmental protection treatment costs, low-value utilization of high-priced elements, and investment in large environmental protection facilities, so as to save chemical raw materials, reduce production costs, and reduce The effect of operating strength

Active Publication Date: 2013-10-30
GRIREM ADVANCED MATERIALS CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in the process of using this method to treat bastnaesite, there are still a large number of high-value non-cerium rare earths entering the cerium-rich slag, resulting in low-value utilization of high-priced elements. Therefore, steps such as alkali decomposition, washing and hydrochloric acid leaching need to be connected. Bastnaesite The comprehensive utilization of fluorine as an associated resource in the treatment process has not been well resolved; fluorine enters the cerium-rich slag during the hydrochloric acid leaching process, and most of it enters the wastewater with alkali conversion, and its environmental protection treatment is extremely difficult.
For the new emission standards for rare earth industrial production, the widely used hydrochloric acid leaching-alkali conversion-re-optimizing leaching process is difficult to meet the new environmental protection requirements, which requires enterprises to invest more in environmental protection facilities and greatly increase environmental protection treatment costs

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] The 65% REO bastnasite was oxidized and roasted at 600 °C for 0.5 h. During the roasting process, 5wt% sodium sulfate of the amount of bastnaesite was added as a roasting aid, and it was leached with hydrochloric acid at 20 °C for 10 h. During the leaching process, 0.1 wt% of cerium sulfate in the amount of bastnaesite was added as a catalytic leaching aid to obtain a cerium-less rare earth chloride solution and a fluorine-containing cerium-rich slag. The leaching rate of rare earth reaches 72.3%, among which the leaching rate of non-cerium rare earth in bastnaesite reaches 98.5%. CeO in fluorine-containing cerium-rich slag 2 / TREO reached 98.4%. The fluorine-containing cerium-rich slag is separated by hydrocyclone to obtain rare earth fluoride with a purity of 96.7%, of which CeO 2 / TREO is greater than 98%. The total yield of rare earths into rare earth fluorides and rare earth chlorides reached 98.1%. The sodium introduced by the roasting aid can be separated fro...

Embodiment 2

[0036] The 65% REO bastnasite was oxidized and roasted at 350 °C for 5 h. During the roasting process, 0.1 wt% aluminum sulfate with the amount of bastnaesite was added as a roasting aid, and leached with hydrochloric acid at 80 °C for 0.5 h, and then leached in hydrochloric acid. In the process, 5 wt % of lanthanum sulfate in the amount of bastnaesite is added as a catalytic leaching aid to obtain a cerium-less rare earth chloride solution and a fluorine-containing cerium-rich slag. The leaching rate of rare earth reaches 70.8%, among which the leaching rate of non-cerium rare earth in bastnaesite reaches 98.4%. CeO in fluorine-containing cerium-rich slag 2 / TREO reaches over 97.1%. The fluorine-containing cerium-rich slag undergoes a flotation process to obtain rare earth fluorides with a purity of 96.3%, of which CeO 2 / TREO is greater than 98%. The total yield of rare earths into rare earth fluorides and rare earth chlorides reached 98.8%. The aluminum introduced by th...

Embodiment 3

[0038] The bastnaesite was oxidized and roasted at 450 °C for 2.5 hours. During the roasting process, 1wt% of sodium fluoride was added as a roasting aid. The hydrochloric acid was used for leaching at 50 °C for 5 hours. During the hydrochloric acid leaching process 2wt% of aluminum nitrate in the amount of bastnaesite was added as a catalytic leaching aid to obtain a cerium-less rare earth chloride solution and a fluorine-containing cerium-rich slag. The leaching rate of rare earth reaches 73.1%, among which the leaching rate of non-cerium rare earth in bastnaesite reaches 99.1%. CeO in fluorine-containing cerium-rich slag 2 / TREO reached 98.7%. The fluorine-containing cerium-rich slag undergoes a magnetic separation process to obtain rare earth fluorides with a purity of 95.3%, of which CeO 2 / TREO is greater than 98%. The total yield of rare earth entering rare earth fluoride and rare earth chloride reaches more than 99.2%. The non-rare earth elements such as sodium and...

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Abstract

The invention provides a method for comprehensively recycling rare earth and fluorine in a process of treating bastnaesite. The method comprises the steps of: carrying out oxidizing roasting on the bastnaesite, leaching a roasted mixture by adopting hydrochloric acid to obtain a rare earth chloride solution containing less cerium and fluorine-containing and cerium-rich slag, wherein a roasting additive is added in the bastnaesite in the roasting process and / or a catalytic leaching additive is added in the mixture in a hydrochloric acid leaching process; and then separating and recycling rare earth chloride from the fluorine-containing and cerium-rich slag. According to the method provided by the invention, the consumption of a large quantity of chemical raw materials can be reduced, the pollution to the environment in a use process is greatly reduced, and the production cost is also greatly lowered. According to the method, the procedures of multiple times of solid-liquid separation and the like are eliminated, the process is simplified, the manipulation strength is reduced, the rare earth loss is reduced, the rare earth yield is increased, and especially the hydrochloric acid leaching recycling rate of high-valent non-cerium rare earth is increased. The method provided by the invention realizes fluorine-free emission in the whole process, and has the characteristics of low consumption, high efficiency and the like.

Description

technical field [0001] The invention relates to a method for comprehensively recovering rare earth and fluorine in the process of bastnaestite treatment, and belongs to the technical field of rare earth hydrometallurgy. Background technique [0002] Bastnaesite is the rare earth mineral resource with the largest reserves and currently the largest amount of mining and use in the world. At present, about 70% of rare earth raw materials are produced from bastnaesite, which is rich in a large amount of fluorine resources. my country is a big country of rare earths, with very rich bastnaesite mineral resources, such as Inner Mongolia Bayan Obo rare earth mine, Sichuan Mianning rare earth mine, Shandong Weishan rare earth mine, etc., all of which are large-scale rare earth deposits dominated by bastnaesite. my country's rare earth production provides 95% of the global rare earth market demand. Sichuan bastnaesite is the second largest rare earth resource in my country. Its smelti...

Claims

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Application Information

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IPC IPC(8): C22B1/02C22B3/10C22B59/00
CPCC22B1/02C22B3/10C22B59/00Y02P10/20
Inventor 王良士龙志奇崔大立黄小卫于瀛徐旸冯兴亮
Owner GRIREM ADVANCED MATERIALS CO LTD
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