Carbon dioxide sequestration methods using group 2 silicates and chlor-alkali processes
The present invention relates to an energy efficient carbon dioxide sequestration processes whereby Group 2 silicate minerals and CO 2 are converted into limestone and sand using a two-salt thermolytic process that allows for the cycling of heat and chemicals from one step to another.
1. A method of sequestering carbon dioxide produced by a source, comprising:
(a) heating a magnesium chloride salt or a hydrate thereof and water in a first admixture to form (i) magnesium hydroxide, magnesium oxide and/or MgCl(OH) and (ii) hydrogen chloride;
(b) admixing (i) magnesium hydroxide, magnesium oxide and/or MgCl(OH), (ii) CaCl 2 and (iii) carbon dioxide produced by the source in a second admixture under conditions suitable to form (iv) calcium carbonate, (v) a magnesium chloride salt, and (vi) water;
(c) separating the calcium carbonate from the second admixture; and
(d) admixing a Group 2 silicate mineral with hydrogen chloride under conditions suitable to form a Group 2 chloride salt, water, and silicon dioxide, where some the hydrogen chloride in this step is obtained from step (a) and wherein some of the hydrogen chloride is obtained from a chlor-alkali electrolytic cell,
whereby the carbon dioxide is sequestered into a mineral product form.
2. The method of claim 1 , wherein some or all of the hydrogen chloride of step (a) is admixed with water to form hydrochloric acid.
3. The method of claim 1 , where some or all of the magnesium hydroxide, magnesium oxide and/or MgCl(OH) of step (b)(i) is obtained from step (a)(i).
4. The method of claim 1 , where some or all of the water in step (a) is present in the form of a hydrate of the magnesium chloride salt.
5. The method of claim 1 , wherein step (a) occurs in one, two or three chambers.
6. The method of claim 1 , wherein step (a) occurs in one chamber.
7. The method of claim 1 , wherein the magnesium hydroxide, magnesium oxide and/or MgCl(OH) of step (a)(i) is greater than 90% by weight Mg(OH)Cl.
8. The method of claim 1 , wherein the magnesium chloride salt is greater than 90% by weight MgCl 2 .6(H 2 O).
9. The method of claim 1 , wherein step (d) further comprises agitating the Group 2 silicate mineral with the hydrochloric acid.
10. The method of claim 1 , where some or all of the magnesium chloride salt in step (a) is obtained from step (d).
11. The method of claim 1 , further comprising a separation step, wherein the silicon dioxide is removed from the Group 2 chloride salt formed in step (d).
12. The method of claim 1 , where some or all of the water of step (a) is obtained from the water of step (d).
13. The method of claim 1 , wherein the Group 2 silicate mineral of step (d) comprises a Group 2 inosilicate.
14. The method of claim 1 , wherein the Group 2 silicate mineral of step (d) comprises CaSiO 3 .
15. The method of claim 1 , wherein the Group 2 silicate mineral of step (d) comprises MgSiO 3 .
16. The method of claim 1 , wherein the Group 2 silicate mineral of step (d) comprises olivine.
17. The method of claim 1 , wherein the Group 2 silicate mineral of step (d) comprises serpentine.
18. The method of claim 1 , wherein the Group 2 silicate mineral of step (d) comprises sepiolite, enstatite, diopside, and/or tremolite.
19. The method of claim 1 , wherein the Group 2 silicate further comprises mineralized iron and or manganese.
20. The method according to claim 1 , wherein step (b) further comprises admixing CaCl 2 and water to the second admixture.
21. The method according to claim 1 , further comprising:
(e) heating a magnesium chloride salt and water in a third admixture to form (i) magnesium hydroxide, magnesium oxide and/or MgCl(OH) and (ii) hydrogen chloride;
(f) admixing (i) magnesium hydroxide, magnesium oxide and/or MgCl(OH), (ii) CaCl 2 and (iii) carbon dioxide produced by the source in a fourth admixture under conditions suitable to form (iv) calcium carbonate, (v) a magnesium chloride salt, and (vi) water;
(g) separating the calcium carbonate from the fourth admixture; and
(h) admixing a Group 2 silicate mineral with hydrogen chloride under conditions suitable to form a Group 2 chloride salt, water, and silicon dioxide, where some or all of the hydrogen chloride in this step is obtained from step (e),
whereby the carbon dioxide is sequestered into a mineral product form.
22. The method of claim 21 , wherein all of the hydrogen chloride in step (h) is obtained from step (e).
23. The method according to claim 1 , further comprising:
admixing (i) sodium hydroxide produced from the chlor-alkali electrolytic cell, and (ii) the carbon dioxide produced by the source in a fifth admixture under conditions suitable to form (iii) sodium bicarbonate and/or sodium carbonate.