Preparation method of high-purity thorium nitrate
A thorium nitrate, high-purity technology, applied in the field of preparation of high-purity thorium nitrate, can solve the problems of weak complexation ability, increase the number of stripping stages, and affect the extraction capacity of the circulating organic phase, so as to promote stripping and improve stripping rate effect
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Embodiment 1
[0023] Th(NO 3 ) 4 The separation and purification of the solution, in which Th(NO 3 ) 4 ThO in solution 2 93.94%, RE 2 o 3 0.34%, U 3 o 8 0.0055%, Fe 2 o 3 5.02%, TiO 2 0.68%. HNO 3 and NaNO 3 As a salting-out agent, deploy Th(NO 3 ) 4 solution, control [Th 4+ ]=60g / L, [HNO 3 ]=0.3mol / L, [NaNO 3 ]=1.3mol / L; P 350 The extractant was diluted with sulfonated kerosene to a P350 concentration of 25%, countercurrent extraction was used, the ratio was organic phase:water phase=3:1, and the number of extraction stages was 20 to obtain Th-loaded organic phase and raffinate. The raffinate is neutralized and removed with NaOH, and the pH is controlled to be greater than 7. After solid-liquid separation, the neutralized slag and NaNO are obtained 3 solution. NaNO obtained by solid-liquid separation 3 The solution is concentrated by evaporation, cooled and crystallized to obtain NaNO 3 Products, Back to Formulating Salting-Out Agents and NaNO 3 detergent.
[0024] ...
Embodiment 2
[0029] Th(NO 3 ) 4 The separation and purification of the solution, in which Th(NO 3 ) 4 ThO in solution 2 93.94%, RE 2 o 3 0.34%, U 3 o 8 0.0055%, Fe 2 o 3 5.02%, TiO 2 0.68%. HNO 3 and NaNO 3 As a salting-out agent, deploy Th(NO 3 ) 4 solution, control [Th 4+ ]=80g / L, [HNO 3 ]=0.5mol / L, [NaNO 3 ]=1.6mol / L; P 350 The extractant was diluted with sulfonated kerosene to a P350 concentration of 30%, countercurrent extraction was used, the ratio was organic phase:water phase=2:1, and the number of extraction stages was 25 to obtain Th-loaded organic phase and raffinate. The raffinate is neutralized and removed with NaOH, and the pH is controlled to be greater than 7. After solid-liquid separation, the neutralized slag and NaNO are obtained 3 solution. NaNO obtained by solid-liquid separation 3 The solution is concentrated by evaporation, cooled and crystallized to obtain NaNO 3 Products, Back to Formulating Salting-Out Agents and NaNO 3 detergent.
[0030] ...
Embodiment 3
[0032] Th(NO 3 ) 4 The separation and purification of the solution, in which Th(NO 3 ) 4 ThO in solution 2 93.94%, RE 2 o 3 0.34%, U 3 o 8 0.0055%, Fe 2 o 3 5.02%, TiO 2 0.68%. HNO 3 and NaNO 3 As a salting-out agent, deploy Th(NO 3 ) 4 solution, control [Th 4+ ]=70g / L, [HNO 3 ]=0.4mol / L, [NaNO 3 ]=1.5mol / L; P 350 The extractant was diluted with sulfonated kerosene to a P350 concentration of 20%, countercurrent extraction was used, the ratio was organic phase:water phase=3:1, and the number of extraction stages was 25 to obtain Th-loaded organic phase and raffinate. The raffinate is neutralized and removed with NaOH, and the pH is controlled to be greater than 7. After solid-liquid separation, the neutralized slag and NaNO are obtained 3 solution. NaNO obtained by solid-liquid separation 3 The solution is concentrated by evaporation, cooled and crystallized to obtain NaNO 3 Products, Back to Formulating Salting-Out Agents and NaNO 3 detergent.
[0033] ...
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