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
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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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