Co-production method for battery-grade lithium carbonate and magnesium based functional materials
A functional material, lithium carbonate technology, applied in chemical instruments and methods, lithium carbonate;/acid carbonate, inorganic chemistry, etc., can solve the problems of complex process, high cost of magnesium and lithium separation methods, and high cost, Achieve the effect of shortening the process flow, good industrialization prospects, and reducing forced evaporation
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0064] 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 the Li in this salt lake old brine + The content is 1g / L, and the ratio of magnesium to lithium is 100.
[0065] 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.
[0066] 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.
[0067] In the second step, the lithium-rich solution enters the reverse osmosis system for primary concentration to obtain a primary concentrate.
[0068] Among them, Li in the primary concentrate + The content is 1.5g / L, and the ratio of magnesium to lithium is 0.01.
[0069] In the third step, the primary co...
Embodiment 2
[0078] 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 the Li in this salt lake old brine + The content is 10g / L, and the ratio of magnesium to lithium is 5.
[0079] 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.
[0080] 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.
[0081] In the second step, the lithium-rich solution enters the reverse osmosis system for primary concentration to obtain a primary concentrate.
[0082] Among them, Li in the primary concentrate + The content is 7.5g / L, and the ratio of magnesium to lithium is 0.4.
[0083] In the third step, the primary conce...
Embodiment 3
[0092] 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 the Li in this salt lake old brine + The content is 7g / L, and the ratio of magnesium to lithium is 8.
[0093] 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.
[0094] Among them, Li in the diluted brine obtained after dilution + The content is 0.7g / L; and Li in the obtained lithium-rich solution + The content is 3g / L, and the ratio of magnesium to lithium is 1.
[0095] In the second step, the lithium-rich solution enters the reverse osmosis system for primary concentration to obtain a primary concentrate.
[0096] Among them, Li in the primary concentrate + The content is 8g / L, and the ratio of magnesium to lithium is 1.
[0097] In the third step, the primary concentrated...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More