Carbon dioxide mineralization using reject brine

1. A process for carbon dioxide (CO 2 ) mineralization using reject brine, comprising the steps of:

(a) introducing ammonia into a first reaction chamber;

(b) obtaining reject brine discharged from a desalination plant, the reject brine having sodium chloride (NaCl);

(c) mixing the reject brine with the ammonia in the first chamber to form ammoniated brine;

(d) capturing CO 2 emitted from a chemical or power plant wherein the CO 2 is 99.9% pure;

(e) dissolving the captured CO 2 with the ammoniated brine in the first chamber and maintaining a temperature between 25° C. and 40° C. in the first chamber to precipitate sodium bicarbonate (NaHCO 3 ) and form an aqueous ammonium chloride (NH 4 Cl) solution and wherein the % sodium conversion is about 95% or greater;

(f) transferring the aqueous ammonium chloride (NH 4 Cl) solution from the first chamber into a second reaction chamber;

(g) adding calcium oxide (CaO) to the aqueous ammonium chloride (NH 4 Cl) solution in the second chamber to form a calcium chloride solution and ammonia.

2. The process for carbon dioxide mineralization according to claim 1 , wherein the step of dissolving the captured CO 2 with the ammoniated brine further comprises maintaining a temperature of about 30° C. in the first chamber.

3. The process for carbon dioxide mineralization according to claim 1 , wherein the reject brine has an initial sodium concentration ranging from 57,000 to 113,000 ppm.

4. The process for carbon dioxide mineralization according to claim 1 , wherein the reject brine has an initial sodium concentration of about 85,000 ppm.

5. The process for carbon dioxide mineralization according to claim 1 , wherein the step of adding calcium oxide (CaO) to the aqueous ammonium chloride (NH 4 Cl) solution further comprises maintaining a temperature between 90° C. and 100° C. in the second chamber.

6. The process for carbon dioxide mineralization according to claim 1 , wherein at least 90% of the ammonia is released from the aqueous ammonium chloride (NH 4 Cl) solution.

7. The process for carbon dioxide mineralization using reject brine according to claim 1 , wherein at least 99% of the ammonia is released from the aqueous ammonium chloride (NH 4 Cl) solution.

8. The process for carbon dioxide mineralization using reject brine according to claim 1 , further comprising the step of transferring ammonia produced from reaction of the calcium oxide with ammonium chloride from the second chamber back into the first chamber for mixing with additional reject brine.

9. The process for carbon dioxide mineralization using reject brine according to claim 1 , wherein the conversion of CO 2 to NaHCO 3 occurs within about 180 minutes.

10. The process for carbon dioxide mineralization using reject brine according to claim 1 , wherein the conversion of CO 2 to NaHCO 3 occurs within about 150 minutes.

11. The process for carbon dioxide mineralization using reject brine according to claim 1 , wherein the conversion of CO 2 to NaHCO 3 occurs within about 120 minutes.

12. The process for carbon dioxide mineralization using reject brine according to claim 1 , wherein the conversion of CO 2 to NaHCO 3 occurs within about 90 minutes.

13. The process for carbon dioxide mineralization using reject brine according to claim 1 , wherein the CaO is added in mol excess.

14. The process for carbon dioxide mineralization using reject brine according to claim 13 , wherein the CaO is added in 20% mol excess.

15. The process for carbon dioxide mineralization using reject brine according to claim 10 , wherein the NH 4 Cl is added in 7.5% mol excess.