Process for sequestrating carbon in the form of a mineral in which the carbon has oxidation number +3

1. A process for sequestrating carbon in the atmosphere, comprising:

a) concentrating atmospheric CO 2 in a liquid phase, by any of the following: (i) liquefying CO 2 in a liquid phase under pressure up to the supercritical state; (ii) absorbing CO 2 in a polar aprotic liquid, not miscible with water, or miscible with water in various proportions; (iii) absorbing CO 2 in an aqueous phase containing an alcohol and/or an amine; or (iv) absorbing CO 2 in the hydrated form in a solvent, activated by an enzymatic pathway, with the provision that in (iii) and (iv) the resultant absorbed CO 2 is transferred to a water-insoluble ionic liquid medium;

b) electro-reduction of resultant liquified CO 2 from (i), liquid or of resultant absorbed CO 2 , in said polar aprotic liquid from (ii) or of resultant CO 2 from (iii) or from (iv) that has been transferred to the water-insoluble ionic liquid medium, to produce oxalic acid or formic acid in which the carbon changes to oxidation number +3;

c) optionally extracting said oxalic acid or formic acid in an aqueous phase; and

d) mineralization by reacting said oxalic acid or formic acid with a carbonate of an element M, producing a mineral in which the atomic ratio C/M is about 2/1, wherein M is any metallic element with an oxidation number of +2, and C is carbon, and wherein the oxalic acid and formic acid are in an acid or salt form.

2. The process according to claim 1 , wherein in a) concentration in the liquid phase comprises the liquefying of said CO 2 , the liquid CO 2 then being obtained under the said pressure, up to the supercritical state.

3. The process according to claim 2 , in which the electro-reduction b) is carried out in liquid CO 2 under pressure.

4. The process according to claim 3 , wherein mineralization (d) compriese attack of a carbonated mineral by an aqueous solution of said oxalic acid or formic acid.

5. The process according to claim 4 , in which said carbonated mineral comprises a calciferous or magnesia-containing carbonated mineral.

6. The process according to claim 1 , wherein in a) concentration in the liquid phase comprises (ii) the absorbing of the CO 2 in the polar aprotic liquid, not miscible with the water or miscible with the water in various proportions.

7. The process according to claim 1 , wherein in a) the concentrating CO 2 in the liquid phase comprises (ii) said absorbing of CO 2 in an aprotic ionic liquid not miscible with the water or miscible with the water in various proportions.

8. The process according to claim 7 , wherein said ionic liquid comprises 1-butyl-3-methylimidazolium hexafluorophosphate.

9. The process according to claim 1 , wherein in a) concentration in the liquid phase comprises (iii) the absorbing of the CO 2 in the aqueous phase containing the alcohol and/or the amine.

10. The process according to claim 9 , wherein a resultant aqueous solution obtained is transferred by a liquid-liquid extraction process to an ionic liquid medium which is insoluble in water.

11. The process according to claim 1 , wherein in a) concentration in the liquid phase comprises (iv) the absorbing of the CO 2 in the hydrated form being activated by the enzymatic pathway.

12. The process according to claim 11 , wherein a hydration activating enzyme comprises carbonic anhydrase.

13. The process according to claim 12 , wherein a resultant liquid phase obtained in (iv) is then recycled to a process for absorption of CO 2 in an aqueous phase in the presence of an alcohol and/or amine.

14. The process according claim 13 , wherein the aqueous phase obtained is recycled to a liquefaction process of CO 2 under pressure.

15. The process according to claim 1 , in which the electro-reduction b) is carried out at a pH in the range of 3 to 10 and with an anode maintained at a potential of +0.5 to −3.5 volts with respect to a normal hydrogen electrode.

16. The process according to claim 15 , in which the pH is in the range of 3 to 7.

17. The process according to claim 15 , in which the anode used in the electro-reduction is platinum, diamond-doped with boron or carbon doped with nitrogen.

18. The process according to claim 1 , in which the electro-reduction b) is carried out in liquid CO 2 under pressure.

19. The process according to claim 1 , in which a compound from electro-reduction b) comprises said oxalic acid or an oxalate.

20. The process according to claim 19 , in which the oxalic acid or oxalate is re-extracted by an aqueous phase.

21. The process according to claim 1 in which, at the end of a), liquid CO 2 is injected into a subterranean CO 2 store.

22. The process according to claim 21 , in which electro-reduction b) is carried out in the subterranean CO 2 store.

23. The process according to claim 22 , in which said mineral comprises a calciferous or magnesia-containing carbonated mineral.

24. The process according to claim 1 , wherein mineralization (d) comprises attack of a carbonated mineral by an aqueous solution of said oxalic acid or formic acid.

25. The process according to claim 1 , in which the element M is calcium and the mineral produced is Whewellite, CaC 2 O 4 .H 2 O.

26. The process according to claim 1 , in which the mineralization (d) reaction with the carbonate of metal M is effected by bringing an aqueous solution of oxalic acid or formic acid derived from the extraction (c) into contact with a calciferous or magnesia-containing sedimentary rock.

27. The process according to claim 1 , in which a final mineralization comprises injection into a substratum.