Hamartite smelting separation process
A bastnaesite and process technology, applied in the field of bastnaesite smelting and separation, to achieve the effects of simple process flow, green process and improved recovery rate
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Embodiment 1
[0034] Bastnaesite is leached with hydrochloric acid through oxidative roasting to obtain a high-quality slag 1 ton, wherein REO content is 30wt%, CeO 2 / TREO is 60%, the weight content of fluorine is 3.0wt%, ThO 2 The content is 0.1 wt%. Be that the sulfuric acid solution of 2 washes with pH, the chloride ion content in the excellent slag after washing is 0.01%, then at room temperature, be 12: 1 (weight ratio) with the sulfuric acid of 0.5mol / L with liquid-solid ratio, to A fine slag was leached for 10 hours, the rare earth leaching rate was 93%, and the obtained sulfuric acid rare earth solution was 14.4m 3 , wherein the rare earth content is 19.4g / L in terms of REO, of which CeO 2 / TREO is 85%, F - The concentration is 1.9g / L, ThO 2 It is 0.03g / L.
[0035] Rare earth sulfate solution using P 507 and P 204 The synergistic extractant is carried out in accordance with the ratio of 1.5:1 for 5-stage countercurrent extraction, extracting cerium (IV), thorium (IV), and ...
Embodiment 2
[0039] Bastnaesite is leached with hydrochloric acid through oxidative roasting to obtain 1 ton of excellent slag, wherein REO content is 75wt%, CeO 2 / TREO is 85%, fluorine content is 10wt%, ThO 2 Content is 0.8wt%, is 4 sulfuric acid solution with pH, washes, and the chloride ion content in the excellent slag after washing is 0.1%, then under 80 degree, is 5.5 with the sulfuric acid of 4mol / L with liquid-solid ratio: 1 (weight ratio) leaching a high-quality slag, leaching for 1 hour, filtering, washing the filter cake with water, the leaching rate of rare earth is 95%, and the rare earth content in the rare earth sulfate solution obtained is 108g / L in terms of REO, wherein CeO 2 / TREO is 80%, F - The concentration is 14.4g / L, ThO 2 The concentration is 1.15g / L.
[0040] The obtained sulfuric acid rare earth solution adopts P 507 and P 204 The synergistic extractant is subjected to 10-stage countercurrent extraction according to the ratio of 8:1, cerium (IV), thorium (...
Embodiment 3
[0044] Bastnaesite is leached with hydrochloric acid through oxidative roasting to obtain a high-quality slag 1 ton, wherein REO content is 40wt%, CeO 2 / TREO is 85%, fluorine content is 4.5wt%, ThO 2 Content is 0.3wt%, with the sulfuric acid solution that pH is 2, wash, and the chloride ion content in the slag after washing is 0.01%, then under 100 ℃, with the sulfuric acid of 6.0mol / L, liquid-solid ratio is 2 : 1 (weight ratio) leaching a fine slag, leaching 2 hours, filtering, water washing filter cake, the leaching rate of rare earth is 95%, and rare earth content in the sulfuric acid rare earth solution obtained is 158g / L with REO, wherein CeO 2 / TREO is 85%, F - The concentration is 17.8g / L, ThO 2 The concentration is 1.19g / L.
[0045] Rare earth sulfate solution using P 507 Carry out 6-stage countercurrent extraction according to the ratio of 12:1, cerium (IV), thorium (IV), fluorine and iron are extracted into the organic phase, and the trivalent rare earths are le...
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