• Title/Summary/Keyword: 희토류정광

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Decomposition and leaching of Rare earth ore (희토류 광물의 분해 및 침출)

  • Lee, Jin-Yeong;Jeon, Ho-Seok;Kim, Joon-Soo
    • Mineral and Industry
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    • v.23
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    • pp.26-31
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    • 2010
  • 희토류 정광으로부터 첨단산업 원료소재로 수요가 급증하고 있는 고순도 희토류 소재를 제조하기 위한 가장 첫 공정은 침출공정이다. 즉, 희토류 정광으로부터 원소별 희토류 성분을 분리하기 위해서는 용액상태로 전환이 필요한데, 이때 일반적인 산 및 알카리 용액에는 희토류 성분은 침출이 되지 않으므로 강산 또는 강 알카리 조건에서 희토류 정광을 침출 가능한 형태로 변환 시켜주는 분해공정이 선행되며 이후 산 침출에 의해 희토류 성분을 침출하게 된다. 본 고에서는 대표적인 희토류 광물인 모나자이트와 바스트나사이트, 그리고 이 광물의 혼합물 형태로 생산되는 혼합광물에 대한 분해 및 침출공정을 소개하고자 한다.

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Overview on the Technologies for Extraction of Rare Earth Metals (희토류금속(稀土類金屬) 제련기술(製鍊技術) 개요)

  • Park, Hyung-Kyu;Lee, Jin-Young;Cho, Sung-Wook;Kim, Joon-Soo
    • Resources Recycling
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    • v.21 no.3
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    • pp.74-83
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    • 2012
  • Rare earth metals have been made from rare earth compounds which were prepared from rare earth ore concentrates through successive processes such as leaching(i.e. extraction of rare earth elements to liquid media), separation, purification, precipitation. Here, process for treating monazite and bastnasite ore concentrates were briefly reviewed, and metallothermic reduction and fused salt electrolysis methods were introduced as the extraction technologies for rare earth metals.

Decomposition and Leaching of Bastnasite by Sulfation and Recovery of Cerium Hydroxide from Leached Solution (황산화반응에 의한 불탄산염 희토류광(Bastnasite)의 분해, 침출 및 세륨수산화물의 회수)

  • Yoon, Ho-Sung;Kim, Sung-Don;Kim, Chul-Joo;Kim, Jun-Soo;Han, Choon
    • Applied Chemistry for Engineering
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    • v.9 no.3
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    • pp.407-412
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    • 1998
  • This study was carried out to investigate the optimum leaching conditions for the sulfation and water leaching, and separation of cerium from rare earth elements in leached solution by acid-adjusting method. The optimum conditions for the sulfation and water leaching from bastnasite concentrates are that the equivalent ration of sulfuric acid to concentrates is 2.5, calcination temperature and time are $600^{\circ}C$ and 2 hrs respectively, and the pulp density in the water leaching is 9.1%. The yield of rare earth oxide is about 93% at the above condition. The process of recovery of cerium hydroxide from leached solution by acid-adjusting method was carried out as following steps. The first step is the oxidation of the solution at pH 5 by using twice the equivalent of $H_2O_2$ solution as an oxidant. The second step is the precipitation to obtain cerium complex salt and cerium hydroxide after lowering the solution to pH 2. The last step is the oxidation-precipitation by using equivalent of $H_2O_2$ solution. From these results, it was possible to prepare cerium hydroxide with the yield of 60% and the quality of 80%.

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