Method for preparing battery-grade lithium carbonate
A lithium carbonate, battery-level technology, applied in lithium carbonate;/acid carbonate and other directions, can solve the problems of complex process, increase investment cost and equipment energy consumption, high cost, shorten the process flow, improve the industry improve the prospects and reduce the effect of forced evaporation
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[0032] The present invention proposes a kind of preparation method of battery-grade lithium carbonate based on the old salt lake brine with high magnesium-lithium ratio; the preparation method comprises the following steps:
[0033] In step S1, the magnesium and lithium of the old salt lake brine are initially separated.
[0034] The basic composition of the old bittern in the salt lake is as follows: Li + The content is 1g / L~10g / L, the ratio of magnesium to lithium is 5:1~100:1, preferably 8:1~50:1; it can be seen that the salt lake old brine is a kind of salt lake old brine with high magnesium-lithium ratio. halogen.
[0035] It should be noted that, in the present invention, "magnesium-lithium ratio" refers to the mass ratio of magnesium ions to lithium ions.
[0036] Specifically, the old salt lake brine is diluted to obtain diluted brine, and then the obtained diluted brine is separated from magnesium and lithium in a membrane separation system to obtain a lithium-rich ...
Embodiment 1
[0062] The salt lake old brine used in this embodiment comes from the old brine produced by a certain salt lake in Qinghai after potassium extraction, and Li in the old brine of the salt lake + The content is 1g / L, and the ratio of magnesium to lithium is 100.
[0063] In the first step, after diluting the old brine of the salt lake with fresh water, it enters the membrane separation system for magnesium and lithium separation to obtain a lithium-rich solution.
[0064] Among them, Li in the diluted brine obtained after dilution + The content is 0.2g / L; and Li in the obtained lithium-rich solution + The content is 0.6g / L, and the ratio of magnesium to lithium is 0.01.
[0065] In the second step, the lithium-rich solution enters the reverse osmosis system for primary concentration to obtain a primary concentrate.
[0066] Among them, Li in the primary concentrate + The content is 1.5g / L, and the ratio of magnesium to lithium is 0.01.
[0067] In the third step, the primar...
Embodiment 2
[0076] The salt lake old brine used in this embodiment comes from the old brine produced by a certain salt lake in Qinghai after potassium extraction, and Li in the old brine of the salt lake + The content is 10g / L, and the ratio of magnesium to lithium is 5.
[0077] In the first step, after diluting the old brine of the salt lake with fresh water, it enters the membrane separation system for magnesium and lithium separation to obtain a lithium-rich solution.
[0078] Among them, Li in the diluted brine obtained after dilution + The content is 0.8g / L; and Li in the obtained lithium-rich solution + The content is 2g / L, and the ratio of magnesium to lithium is 0.4.
[0079] In the second step, the lithium-rich solution enters the reverse osmosis system for primary concentration to obtain a primary concentrate.
[0080] Among them, Li in the primary concentrate + The content is 7.5g / L, and the ratio of magnesium to lithium is 0.4.
[0081] In the third step, the primary con...
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