METHOD OF ELECTRODEPOSITION IN SEAWATER FOR THE GROWTH OF CONSTRUCTION MATERIALS
The present invention relates to a method to produce calcium rich-based aggregates by electrodeposition in salty aqueous CO 2 enriched solutions, that can be used in the construction industry. The method includes filtering an aqueous salty solution to produce an aqueous salty solution free of organic debris or pollutants, adjusting a temperature and pH in a conditioning reactor CR1 to produce an aqueous salty solution, bringing the aqueous salty solution from CR1 to a continuous reactor CR2 equipped with an electroactive substrate comprising at least one cathode and at least one anode connected to an electrical DC supply, injecting in CR2 a flux of a gas mixture containing CO 2 (C-gas) in contact with the flux of the aqueous solution, applying to the flux of the CO 2 -enriched aqueous solution a constant DC current, and recovering the calcium rich-based aggregates deposited on the electroactive substrate and/or on the bottom of CR2.
1 . Method to produce calcium rich-based aggregates, said method comprising the following steps:
a) Filter an aqueous salty solution AS1 to produce an aqueous salty solution AS2 free of organic debris or pollutants;
b) Bring the aqueous salty solution AS2 at a temperature from 18 to 29° C. and at a pH from 7.1 to 9, in a conditioning reactor CR1 to produce an aqueous salty solution AS3;
c) Bring the aqueous salty solution AS3 from CR1 to a continuous reactor CR2 equipped with an electroactive substrate comprising at least one cathode and at least one anode connected to an electrical DC supply, wherein the flux of AS3 (FRAS3) in CR2 is kept at a velocity or displacement speed VAS3 located from 0.01 m/s to 5 m/s;
d) Inject in CR2 a flux of a gas mixture containing CO 2 (C-gas) in contact with the flux of the aqueous solution AS3;
e) Apply to the flux of the CO 2 -enriched aqueous solution AS3 a constant DC current ranging from 1 A/m 2 to 5000 A/m 2 , the m 2 representing the deployed surface of the electrodes in contact with AS3, or a voltage ranging from 0.5 V to 20.0 V, to the electrodes;
f) Recover the calcium rich-based aggregates deposited on the electroactive substrate and/or on the bottom of CR2.
2 . Method according to claim 1 , wherein the aqueous salty solution AS2 is brought in step b) at a temperature from 20° C. to 25° C. and at a pH from 8.0 to 8.4, in CR1.
3 . Method according to claim 1 , wherein the continuous reactor CR2 of step c) comprises at least two compartments each comprising at least one cathode or at least one anode.
4 . Method according to claim 1 , wherein the C-gas of step d) is re-circulated to be re-injected into CR2.
5 . Method according to claim 1 , wherein the volume % of CO 2 injected in the continuous reactor CR2 in step d) is 0.05-10 volume % per hour.
6 . Method according to claim 1 , wherein the DC current ranges from 5 A/m 2 to 1000 A/m 2 .
7 . Method according to claim 1 , wherein the voltage ranges from 0.8 V to 10.0 V volts.
8 . Method according to claim 1 , wherein the calcium rich-based aggregates are produced with a CaCO 3 content from 20% to 90%.
9 . Method according to claim 1 ; wherein the calcium rich-based aggregates are produced with an average size from 0.1 mm to 15 mm.