LITHIUM RECOVERY FROM LITHIUM-ION BATTERIES
Recycling of charge material for an NMC (Ni, Mn, Co) battery recovers lithium from a recycled battery stream by roasting a black mass from the recycled stream in a partial oxygen environment at a temperature based on the thermal reduction of cathode material and reacting carbon in an anode material with lithium in the cathode material, and then leaching the lithium from the roasted black mass for forming a lithium leach solution. Lithium is recovered by heating the lithium leach solution, precipitating the lithium carbonate based on decreased solubility of the leached lithium carbonate at the increased temperature.
1 . A method for recovering lithium from a recycled battery stream, comprising:
roasting a black mass from the recycled battery stream in a partial oxygen environment at a temperature based on a thermal reduction of the cathode material;
leaching the lithium from the black mass to form a lithium leach solution; and
heating the lithium leach solution to recover the lithium as a precipitate.
2 . The method of claim 1 , wherein the partial oxygen environment has a lower concentration of oxygen than atmospheric oxygen and a nitrogen concentration greater than atmospheric nitrogen.
3 . The method of claim 2 , wherein the partial oxygen environment comprises 2-10% oxygen.
4 . The method of claim 3 , wherein the partial oxygen environment comprises 3-5% oxygen.
5 . The method of claim 2 , wherein the partial oxygen environment comprises greater than 80% of an inert gas.
6 . The method of claim 5 , wherein the inert gas is nitrogen.
7 . The method of claim 1 , wherein the temperature for roasting the black mass is from 500° C. to 700° C.
8 . The method of claim 7 , wherein the temperature for roasting the black mass is from 575° C. to 650° C.
9 . The method of claim 1 , wherein the black mass is roasted for 10-120 minutes.
10 . The method of claim 9 , wherein the black mass is roasted for 30-60 minutes.
11 . The method of claim 1 , wherein the black mass is leached with water.
12 . The method of claim 11 , wherein the black mass and the water are in a weight ratio of 5-40.
13 . The method of claim 12 , wherein the weight ratio is 15-20.
14 . The method of claim 1 , wherein the black mass is leached at a temperature of 5° C. to 40° C.
15 . The method of claim 14 , wherein the black mass is leached at a temperature of 5° C. to 25° C.
16 . The method of claim 1 , wherein the precipitate is lithium carbonate.
17 . The method of claim 1 further comprising purifying the recovered lithium precipitate by:
combining carbon dioxide with the recovered lithium precipitate for selective dissolution of lithium carbonate by converting highly soluble lithium bicarbonate in water to form a carbonated solution, and
filtering undissolved impurity solids.
18 . The method of claim 17 , wherein the carbonated solution comprises lithium bicarbonate.
19 . The method of claim 18 , further comprising:
heating the carbonated solution to a temperature of greater than 90° C. to form a purified lithium carbonate solid, and
filtering to remove the purified lithium carbonate solid.
20 . The method of claim 1 wherein heating the lithium leach solution precipitates lithium based on decreased solubility of the leached lithium at the increased temperature.
21 . A method of producing purified, battery grade lithium carbonate from a black mass of an Li-ion battery recycling stream, comprising:
heating a black mass from the recycling stream in a partial oxygen environment including 3-5% oxygen balanced by nitrogen at a temperature between 575° C. and 650° C. for a duration between 15 and 60 minutes to generate a roasted black mass;
leaching the roasted black mass in deionized water at a temperature between 5° C.-25° C. at a water ratio of between 15-20 while agitating for 20-60 minutes to form a lithium leach solution;
filtering the lithium leach solution for removal of unleached solids;
harvesting lithium carbonate from the lithium leach solution by heating to a temperature greater than 90° C. for at least 30 minutes for separating Li 2 CO 3 solids based on decreased solubility at higher temperatures;
dissolving the separated Li 2 CO 3 solids in a carbonized, deionized water solution for filtering impurities as solids; and
heating the filtered, carbonized deionized water solution for precipitating purified lithium carbonate as temperature increases to greater than 90° C.