A liquid-liquid extraction process for separating lithium isotopes
A lithium isotope and process technology, applied in the separation of different isotopic elements, separation methods, separation of dispersed particles, etc., can solve problems such as mercury volatile loss, large amounts of mercury, and environmental hazards around operators
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Embodiment 1
[0103] Connect the pipelines according to the process diagram, and a total of 20 centrifugal extractors are used in the extraction and separation C1 section and the extraction and separation C2 section. Buffer H1 section contains the first liquid storage tank with a volume of 0.018m 3 ;The buffer H2 section contains the second liquid storage tank with a volume of 0.001m 3 .
[0104] Organic phase: Contains 7-trifluoromethyl-10-hydroxybenzoquinoline, and co-extractant and diluent.
[0105] Phase inversion liquid aqueous phase (A1): NaCl aqueous solution.
[0106] Conditioning solution (T): Sodium hydroxide aqueous solution.
[0107] Lithium-containing liquid (F): Li 2 SO 4 Aqueous solution, 1.8mol / L, in which the abundance of lithium-6 is 7.49%, and the abundance of lithium-7 is 92.51%.
[0108] The organic phase and each aqueous phase are added through the feeding pump, and the entire extraction process is run. After 156 hours, the system reaches equilibrium, and continu...
Embodiment 2
[0111] The technical process and the feed liquid all adopt the parameters in Example 1, and only change the volume of the first liquid storage tank in the buffer H1 section to 0.040m 3 . Can be continuously separated to obtain enrichment products different from the abundance values in Example 1:
[0112] The lithium-6 abundance value of the lithium-6 enrichment product (P1) is 8.03%, and the stage efficiency of the extraction and separation C1 section is 94%; the lithium-7 abundance value of the lithium-7 enrichment product (P2) is 93.90 %, the stage efficiency of the extraction and separation C2 section is 95%.
Embodiment 3
[0114] Connect the pipelines according to the process diagram, use 45 centrifugal extractors for the extraction and separation C1 section, and 160 centrifugal extractors for the extraction and separation C2 section. Buffer H1 section and buffer H2 section contain liquid storage tanks.
[0115] Organic phase: Contains 10-hydroxybenzoquinoline.
[0116] Phase inversion liquid water phase (A1): Na 2 SO 4 aqueous solution.
[0117] Conditioning solution (T): Potassium hydroxide aqueous solution.
[0118] Lithium-containing liquid (F): Li 2 SO 4 Aqueous solution, 2.5mol / L, in which the abundance of lithium-6 is 7.49%, and the abundance of lithium-7 is 92.51%.
[0119] The organic phase and each aqueous phase are added through the feeding pump, and the entire extraction process is run. After the system reaches equilibrium, continuous separation and two enriched products are obtained at the same time:
[0120] The lithium-6 abundance value of the lithium-6 enrichment product (...
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