Processes for preparing highly pure lithium carbonate and other highly pure lithium containing compounds
The invention generally relates to methods of selectively removing lithium from various liquids, methods of producing high purity lithium carbonate, methods of producing high purity lithium hydroxide, and methods of regenerating resin.
1. A method of producing high purity lithium carbonate, comprising the steps of:
reacting a first aqueous solution comprising a technical grade Li 2 CO 3 with CO 2 to form a second aqueous solution comprising dissolved LiHCO 3 ;
separating unreacted CO 2 and insoluble compounds from the second aqueous solution using a gas-liquid-solid separator to produce a third aqueous solution,
supplying the third aqueous solution to a reverse osmosis apparatus to concentrate the Li 2 CO 3 , wherein the reverse osmosis apparatus is operable to remove CO2 from the solution;
removing dissolved impurities from the third aqueous solution by contacting the third aqueous solution with an ion selective medium to produce a fourth aqueous solution; and
precipitating Li 2 CO 3 from the fourth aqueous solution, wherein the Li 2 CO 3 has a purity of at least about 99.99%.
2. The method according to claim 1 , wherein the insoluble compounds separated from the second aqueous solution are recycled to the first aqueous solution.
3. The method according to claim 1 , further comprising the step of preheating the third aqueous solution to a temperature of 50° C. before precipitating Li 2 CO 3 .
4. A method of producing high purity lithium carbonate, comprising the steps of:
contacting an aqueous brine containing LiHCO 3 having a purity of less than about 99% with CO 2 at ambient temperature to form a second aqueous solution comprising LiHCO 3 and dissolved ions;
supplying the second aqueous solution to a reverse osmosis apparatus, wherein said reverse osmosis apparatus is configured to operate at high pressures, thereby concentrating the Li 2 CO 3 ;
separating insoluble compounds from the second aqueous solution using a gas-liquid-solid reactor to form a third aqueous solution, the third aqueous solution comprising LiHCO 3 and dissolved ions;
extracting at least a portion of the dissolved ions from said third aqueous solution with an ion selective medium to form a fourth aqueous solution containing the dissolved LiHCO 3 and having a reduced concentration of dissolved ions relative to the third aqueous solution;
maintaining a constant pressure while carrying out the separating and extracting steps; and
heating the fourth aqueous solution to form solid LiHCO 3 , gaseous CO 2 and dissolved impurities.
5. The method according to claim 4 , wherein the insoluble compounds separated from the second aqueous solution are recycled to the first aqueous solution.
6. A method of producing highly pure LiPF 6 , the method comprising the steps of:
reacting a first aqueous solution comprising a technical grade Li 2 CO 3 with CO 2 to form a second aqueous solution comprising dissolved LiHCO 3 ;
separating unreacted CO 2 and insoluble compounds from the second aqueous solution using a gas-liquid-solid separator to produce a third aqueous solution,
supplying the third aqueous solution to a reverse osmosis apparatus to concentrate the Li 2 CO 3 , wherein the reverse osmosis apparatus is operable to remove CO 2 from the solution;
removing dissolved impurities from the third aqueous solution by contacting the third aqueous solution with an ion selective medium to produce a fourth aqueous solution;
precipitating Li 2 CO 3 having a purity of at least 99.99% from the fourth aqueous solution;
reacting the Li 2 CO 3 having a purity of at least 99.99% with HF to produce lithium fluoride solution; and
reacting the solution with PF 5 to produce LiPF 6 .
7. A method of producing highly pure LiF, the method comprising the steps of:
reacting a first aqueous solution comprising a technical grade Li 2 CO 3 with CO 2 to form a second aqueous solution comprising dissolved LiHCO 3 ;
separating unreacted CO 2 and insoluble compounds from the second aqueous solution using a gas-liquid-solid separator to produce a third aqueous solution,
supplying the third aqueous solution to a reverse osmosis apparatus to concentrate the Li 2 CO 3 , wherein the reverse osmosis apparatus is operable to remove CO 2 from the solution;
removing dissolved impurities from the third aqueous solution by contacting the third aqueous solution with an ion selective medium to produce a fourth aqueous solution;
precipitating Li 2 CO 3 from the fourth aqueous solution; and
reacting the high purity lithium carbonate having a purity of at least 99.99% with HF gas in a fluidized bed reactor to produce LiF, wherein the LiF is highly pure and dry.
8. A method of producing highly pure LiMnO 2 , the method comprising the steps of:
reacting a first aqueous solution comprising a technical grade Li 2 CO 3 with CO 2 to form a second aqueous solution comprising dissolved LiHCO 3 ;
separating unreacted CO 2 and insoluble compounds from the second aqueous solution using a gas-liquid-solid separator to produce a third aqueous solution,
supplying the third aqueous solution to a reverse osmosis apparatus to concentrate the Li 2 CO 3 , wherein the reverse osmosis apparatus is operable to remove CO 2 from the solution;
removing dissolved impurities from the third aqueous solution by contacting the third aqueous solution with an ion selective medium to produce a fourth aqueous solution;
precipitating Li 2 CO 3 from the fourth aqueous solution; and
reacting high purity lithium carbonate having a purity of at least 99.99% with electrolytic MnO 2 to produce high purity LiMnO 2 .
9. A method of producing highly pure lithium cobalt oxide, the method comprising the steps of:
reacting a first aqueous solution comprising a technical grade Li 2 CO 3 with CO 2 to form a second aqueous solution comprising dissolved LiHCO 3 ;
separating unreacted CO 2 and insoluble compounds from the second aqueous solution using a gas-liquid-solid separator to produce a third aqueous solution,
supplying the third aqueous solution to a reverse osmosis apparatus to concentrate the Li 2 CO 3 , wherein the reverse osmosis apparatus is operable to remove CO 2 from the solution;
removing dissolved impurities from the third aqueous solution by contacting the third aqueous solution with an ion selective medium to produce a fourth aqueous solution;
precipitating Li 2 CO 3 from the fourth aqueous solution; and
reacting the lithium carbonate having a purity of at least about 99.99% with cobalt oxide to produce high purity lithium cobalt oxide.
10. A method of producing highly pure lithium iron phosphate, the method comprising the steps of:
reacting a first aqueous solution comprising a technical grade Li 2 CO 3 with CO 2 to form a second aqueous solution comprising dissolved LiHCO 3 ;
separating unreacted CO 2 and insoluble compounds from the second aqueous solution using a gas-liquid-solid separator to produce a third aqueous solution,
supplying the third aqueous solution to a reverse osmosis apparatus to concentrate the Li 2 CO 3 , wherein the reverse osmosis apparatus is operable to remove CO 2 from the solution;
removing dissolved impurities from the third aqueous solution by contacting the third aqueous solution with an ion selective medium to produce a fourth aqueous solution;
precipitating Li 2 CO 3 from the fourth aqueous solution; and
reacting the lithium carbonate having a purity of at least about 99.99% with high purity ferric phosphate to produce high purity lithium iron phosphate.
11. A method of producing highly pure LiH 2 PO 4 , the method comprising the steps of:
reacting a first aqueous solution comprising a technical grade Li 2 CO 3 with CO 2 to form a second aqueous solution comprising dissolved LiHCO 3 ;
separating unreacted CO 2 and insoluble compounds from the second aqueous solution using a gas-liquid-solid separator to produce a third aqueous solution,
supplying the third aqueous solution to a reverse osmosis apparatus to concentrate the Li 2 CO 3 , wherein the reverse osmosis apparatus is operable to remove CO 2 from the solution;
removing dissolved impurities from the third aqueous solution by contacting the third aqueous solution with an ion selective medium to produce a fourth aqueous solution;
precipitating Li 2 CO 3 from the fourth aqueous solution; and
reacting the lithium carbonate having a purity of at least about 99.99% with phosphoric acid to produce highly pure LiH 2 PO 4 .
12. The method of claim 11 , further comprising the step of reacting the highly pure LiH 2 PO 4 with iron oxide to produce lithium iron phosphate.
13. A method of producing highly pure lithium chloride, the method comprising the steps of:
reacting a first aqueous solution comprising a technical grade Li 2 CO 3 with CO 2 to form a second aqueous solution comprising dissolved LiHCO 3 ;
separating unreacted CO 2 and insoluble compounds from the second aqueous solution using a gas-liquid-solid separator to produce a third aqueous solution,
supplying the third aqueous solution to a reverse osmosis apparatus to concentrate the Li 2 CO 3 , wherein the reverse osmosis apparatus is operable to remove CO 2 from the solution;
removing dissolved impurities from the third aqueous solution by contacting the third aqueous solution with an ion selective medium to produce a fourth aqueous solution;
precipitating Li 2 CO 3 from the fourth aqueous solution; and
reacting a solution comprising deionized water and the lithium carbonate having a purity of at least about 99.99% with gaseous hydrochloric acid to produce highly pure lithium chloride.
14. A method of producing highly pure electrolyte salts, the method comprising the steps of:
reacting a first aqueous solution comprising a technical grade Li 2 CO 3 with CO 2 to form a second aqueous solution comprising dissolved LiHCO 3 ;
separating unreacted CO 2 and insoluble compounds from the second aqueous solution using a gas-liquid-solid separator to produce a third aqueous solution,
supplying the third aqueous solution to a reverse osmosis apparatus to concentrate the Li 2 CO 3 , wherein the reverse osmosis apparatus is operable to remove CO 2 from the solution;
removing dissolved impurities from the third aqueous solution by contacting the third aqueous solution with an ion selective medium to produce a fourth aqueous solution;
precipitating Li 2 CO 3 from the fourth aqueous solution; and
reacting the lithium carbonate having a purity of at least about 99.99% by either triflation or perchloration and using LiASF 5 , LiBF 3 , lithium bis(oxalate)borate, or combinations thereof to produce highly pure electrolyte salts.
15. A method of producing highly pure LiF, the method comprising the steps of:
contacting an aqueous brine containing LiHCO 3 having a purity of less than about 99% with CO 2 at ambient temperature to form a second aqueous solution comprising LiHCO 3 and dissolved ions;
supplying the second aqueous solution to a reverse osmosis apparatus, wherein said reverse osmosis apparatus is configured to operate at high pressures, thereby concentrating the Li 2 CO 3 ;
separating insoluble compounds from the second aqueous solution using a gas-liquid-solid reactor to form a third aqueous solution, the third aqueous solution comprising LiHCO 3 and dissolved ions;
extracting at least a portion of the dissolved ions from said third aqueous solution with an ion selective medium to form a fourth aqueous solution containing the dissolved LiHCO 3 and having a reduced concentration of dissolved ions relative to the third aqueous solution;
maintaining a constant pressure while carrying out the separating and extracting steps;
heating the fourth aqueous solution to form solid LiHCO 3 , gaseous CO 2 and dissolved impurities; and
reacting the high purity lithium carbonate with HF gas in a fluidized bed reactor, wherein the LiF is highly pure and dry.
16. A method of producing highly pure LiMnO 2 , the method comprising the steps of:
contacting an aqueous brine contain in LiHCO 3 having a purity of less than about 99% with CO 2 at ambient temperature to form a second aqueous solution comprising LiHCO 3 and dissolved ions;
supplying the second aqueous solution to a reverse osmosis apparatus, wherein said reverse osmosis apparatus is configured to operate at high pressures, thereby concentrating the Li 2 CO 3 ;
separating insoluble compounds from the second aqueous solution using a gas-liquid-solid reactor to form a third aqueous solution, the third aqueous solution comprising LiHCO 3 and dissolved ions;
extracting at least a portion of the dissolved ions from said third aqueous solution with an ion selective medium to form a fourth aqueous solution containing the dissolved LiHCO 3 and having a reduced concentration of dissolved ions relative to the third aqueous solution;
maintaining a constant pressure while carrying out the separating and extracting steps;
heating the fourth aqueous solution to form solid LiHCO 3 gaseous CO 2 and dissolved impurities; and
reacting the high purity lithium carbonate with electrolytic MnO 2 to produce high purity LiMnO 2 .
17. A method of producing highly pure lithium cobalt oxide, the method comprising the steps of:
contacting an aqueous brine containing LiHCO 3 having a purity of less than about 99% with CO 2 at ambient temperature to form a second aqueous solution comprising LiHCO 3 and dissolved ions;
supplying the second aqueous solution to a reverse osmosis apparatus, wherein said reverse osmosis apparatus is configured to operate at high pressures, thereby concentrating the Li 2 CO 3 ;
separating insoluble compounds from the second aqueous solution using a gas-liquid-solid reactor to form a third aqueous solution, the third aqueous solution comprising LiHCO 3 and dissolved ions;
extracting at least a portion of the dissolved ions from said third aqueous solution with an ion selective medium to form a fourth aqueous solution containing the dissolved LiHCO 3 and having a reduced concentration of dissolved ions relative to the third aqueous solution;
maintaining a constant pressure while carrying out the separating and extracting steps;
heating the fourth aqueous solution to form solid LiHCO 3 , gaseous CO 2 and dissolved impurities; and
reacting high purity lithium carbonate with cobalt oxide to produce high purity lithium cobalt oxide.
18. A method of producing highly pure lithium iron phosphate, the method comprising the steps of:
contacting an aqueous brine containing LiHCO 3 having a purity of less than about 99% with CO 2 at ambient temperature to form a second aqueous solution comprising LiHCO 3 and dissolved ions;
supplying the second aqueous solution to a reverse osmosis apparatus, wherein said reverse osmosis apparatus is configured to operate at high pressures, thereby concentrating the Li 2 CO 3 ;
separating insoluble compounds from the second aqueous solution using a gas-liquid-solid reactor to form a third aqueous solution, the third aqueous solution comprising LiHCO 3 and dissolved ions;
extracting at least a portion of the dissolved ions from said third aqueous solution with an ion selective medium to form a fourth aqueous solution containing the dissolved LiHCO 3 and having a reduced concentration of dissolved ions relative to the third aqueous solution;
maintaining a constant pressure while carrying out the separating and extracting steps;
heating the fourth aqueous solution to form solid LiHCO 3 , gaseous CO 2 and dissolved impurities; and
reacting the high purity lithium carbonate with high purity ferric phosphate to produce high purity lithium iron phosphate.
19. A method of producing highly pure LiH 2 PO 4 , the method comprising the steps of:
contacting an aqueous brine containing LiHCO 3 having a purity of less than about 99% with CO 2 at ambient temperature to form a second aqueous solution comprising LiHCO 3 and dissolved ions;
supplying the second aqueous solution to a reverse osmosis apparatus, wherein said reverse osmosis apparatus is configured to operate at high pressures, thereby concentrating the Li 2 CO 3 ;
separating insoluble compounds from the second aqueous solution using a gas-liquid-solid reactor to form a third aqueous solution, the third aqueous solution comprising LiHCO 3 and dissolved ions;
extracting at least a portion of the dissolved ions from said third aqueous solution with an ion selective medium to form a fourth aqueous solution containing the dissolved LiHCO 3 and having a reduced concentration of dissolved ions relative to the third aqueous solution;
maintaining a constant pressure while carrying out the separating and extracting steps;
heating the fourth aqueous solution to form solid LiHCO 3 , gaseous CO 2 and dissolved impurities; and
reacting the high purity lithium carbonate with phosphoric acid to produce highly pure LiH 2 PO 4 .
20. The method of claim 19 , further comprising the step of reacting the highly pure LiH 2 PO 4 with iron oxide to produce lithium iron phosphate.
21. A method of producing highly pure lithium chloride, the method comprising the steps of:
contacting an aqueous brine containing LiHCO 3 having a purity of less than about 99% with CO 2 at ambient temperature to form a second aqueous solution comprising LiHCO 3 and dissolved ions;
supplying the second aqueous solution to a reverse osmosis apparatus, wherein said reverse osmosis apparatus is configured to operate at high pressures, thereby concentrating the Li 2 CO 3 ;
separating insoluble compounds from the second aqueous solution using a gas-liquid-solid reactor to form a third aqueous solution, the third aqueous solution comprising LiHCO 3 and dissolved ions;
extracting at least a portion of the dissolved ions from said third aqueous solution with an ion selective medium to form a fourth aqueous solution containing the dissolved LiHCO 3 and having a reduced concentration of dissolved ions relative to the third aqueous solution;
maintaining a constant pressure while carrying out the separating and extracting steps;
heating the fourth aqueous solution to form solid LiHCO 3 , gaseous CO 2 and dissolved impurities; and
reacting a solution comprising deionized water and the high purity lithium carbonate with gaseous hydrochloric acid to produce highly pure lithium chloride.
22. A method of producing highly pure electrolyte salts, the method comprising the steps of:
contacting an aqueous brine containing LiHCO 3 having a purity of less than about 99% with CO 2 at ambient temperature to form a second aqueous solution comprising LiHCO 3 and dissolved ions;
supplying the second aqueous solution to a reverse osmosis apparatus, wherein said reverse osmosis apparatus is configured to operate at high pressures, thereby concentrating the Li 2 CO 3 ;
separating insoluble compounds from the second aqueous solution using a gas-liquid-solid reactor to form a third aqueous solution, the third aqueous solution comprising LiHCO 3 and dissolved ions;
extracting at least a portion of the dissolved ions from said third aqueous solution with an ion selective medium to form a fourth aqueous solution containing the dissolved LiHCO 3 and having a reduced concentration of dissolved ions relative to the third aqueous solution;
maintaining a constant pressure while carrying out the separating and extracting steps;
heating the fourth aqueous solution to form solid LiHCO 3 , gaseous CO 2 and dissolved impurities; and
reacting high purity lithium carbonate by either triflation or perchloration and using LiASF 5 , LiBF 3 , lithium bis(oxalate)borate, or combinations thereof to produce highly pure electrolyte salts.