Carbon dioxide mineralization and storage
Carbon dioxide may be stored in a subterranean formation. Methods of subterranean carbon dioxide storage may include: introducing, through an injection region of a unified wellbore to a subterranean formation, a carbonated aqueous fluid including carbon dioxide dispersed within an aqueous fluid, wherein the subterranean formation includes a basaltic formation; reacting the carbon dioxide or an ion thereof with the basaltic formation to form mineralized carbon and a produced aqueous fluid; flowing a mixture of the carbonated aqueous fluid and the produced aqueous fluid through a delivery region of the unified wellbore; depositing the mineralized carbon dioxide within the subterranean formation; and flowing the produced aqueous fluid from the subterranean formation through a production region of the unified wellbore, wherein the injection region and the production region are substantially vertical, and wherein the delivery region is substantially horizontal.
1 . A method comprising:
providing a carbonated aqueous fluid comprising carbon dioxide dispersed within an aqueous fluid;
introducing the carbonated aqueous fluid to a subterranean formation via a unified wellbore comprising an injection region and a production region that are connected by a delivery region that is contiguous with and extends continuously between the injection region and the production region, the carbonated aqueous fluid being introduced through the injection region and entering the delivery region;
wherein the injection region, the production region, and the delivery region each have wellbore diameters that are within 25% of each other; and
wherein the subterranean formation comprises a basaltic formation;
reacting the carbon dioxide or an ion thereof with the basaltic formation, as the carbonated aqueous fluid flows through the delivery region and is maintained therein for a shut-in time, wherein, during the shut-in time, flow within the unified wellbore is interrupted, thus contacting one or more unified wellbore walls along the entire length thereof, to form mineralized carbon and a produced aqueous fluid;
flowing a mixture of the carbonated aqueous fluid and the produced aqueous fluid through the delivery region to the production region;
depositing the mineralized carbon within the subterranean formation; and
flowing the produced aqueous fluid received from the delivery region through the production region, the produced aqueous fluid exiting the subterranean formation via the production region;
wherein the injection region and the production region are substantially vertical, and the delivery region is substantially horizontal.
2 . The method of claim 1 , wherein the delivery region has a length of about 5,000 ft to about 7,000 ft.
3 . The method of claim 1 , further comprising: carbonating the produced aqueous fluid such that the produced aqueous fluid is converted to a recycled carbonated aqueous fluid; and
re-introducing the recycled carbonated aqueous fluid to the subterranean formation along with the carbonated aqueous fluid.
4 . The method of claim 1 , wherein the basaltic formation comprises a mineral of at least one of calcium, magnesium, or iron.
5 . The method of claim 1 , wherein the shut-in time is from about 1 hour to about 90 days.
6 . The method of claim 1 , wherein the carbon dioxide is at least partially dissolved within the aqueous fluid.
7 . The method of claim 1 , wherein the carbonated aqueous fluid has total dissolved solids of about 100 parts per million (ppm) to about 250,000 ppm.
8 . The method of claim 1 , wherein a quantity of the carbon dioxide introduced to the subterranean formation is in excess of a stoichiometric quantity needed to completely react with the basaltic formation to form the mineralized carbon.
9 . The method of claim 1 , wherein the mineralized carbon comprises a carbonate compound selected from the group consisting of calcium carbonate, magnesium carbonate, ferrous carbonate, and combinations thereof.
10 . The method of claim 1 , wherein the reacting occurs at a pressure of about 0.3 MPa to about 11 MPa.
11 . The method of claim 1 , further comprising: adding an acidizing agent, a surfactant, a kinetic inhibitor, or any combination thereof, to the provided carbonated aqueous fluid, such that, during the reacting step, a blockage of channels of the one or more unified wellbore walls is at least partially reduced or mitigated.
12 . A method comprising:
providing a carbonated aqueous fluid comprising carbon dioxide dispersed within an aqueous fluid;
introducing the carbonated aqueous fluid to a subterranean formation via a unified wellbore comprising an injection region and a production region that are connected by a delivery region that is contiguous with and extends continuously between the injection region and the production region, the carbonated aqueous fluid being introduced through the injection region and entering the delivery region;
wherein the injection region, the production region, and the delivery region each have wellbore diameters that are within 25% of each other; and
wherein the subterranean formation comprises a basaltic formation;
reacting the carbon dioxide or an ion thereof with the basaltic formation, as the carbonated aqueous fluid flows through the delivery region and is maintained therein for a residence time, wherein, during the residence time, flow within the unified wellbore is not interrupted, thus contacting one or more unified wellbore walls along the entire length thereof, to form mineralized carbon and a produced aqueous fluid;
flowing a mixture of the carbonated aqueous fluid and the produced aqueous fluid through the delivery region to the production region;
depositing the mineralized carbon within the subterranean formation;
flowing the produced aqueous fluid received from the delivery region through the production region, the produced aqueous fluid exiting the subterranean formation via the production region;
wherein the injection region and the production region are substantially vertical, and the delivery region is substantially horizontal;
carbonating the produced aqueous fluid such that the produced aqueous fluid is converted to a recycled carbonated aqueous fluid; and
re-introducing the recycled carbonated aqueous fluid to the subterranean formation along with the carbonated aqueous fluid.
13 . The method of claim 12 , wherein the delivery region has a length of about 5,000 ft to about 7,000 ft.
14 . The method of claim 12 , wherein the basaltic formation comprises a mineral of at least one of calcium, magnesium, or iron.
15 . The method of claim 12 , wherein the residence time is from about 1 hour to about 90 days.
16 . The method of claim 12 , wherein the carbonated aqueous fluid has total dissolved solids of about 100 parts per million (ppm) to about 250,000 ppm.
17 . The method of claim 12 , wherein a quantity of the carbon dioxide introduced to the subterranean formation is in excess of a stoichiometric quantity needed to completely react with the basaltic formation to form the mineralized carbon.
18 . The method of claim 12 , wherein the mineralized carbon comprises a carbonate compound selected from the group consisting of calcium carbonate, magnesium carbonate, ferrous carbonate, and combinations thereof.
19 . The method of claim 12 , further comprising: adding an acidizing agent, a surfactant, a kinetic inhibitor, or any combination thereof, to the provided carbonated aqueous fluid, such that, during the reacting step, a blockage of channels of the one or more unified wellbore walls is at least partially reduced or mitigated.