System and method for using carbon dioxide sequestered from seawater in the remineralization of process water

1. A method for remineralizing process water in a seawater desalination plant, seawater used in the plant containing bicarbonate, the method comprising the following steps:

providing a desalination system including an upstream inlet for the seawater and downstream outlets for desalinated water and concentrate;

providing a gas transfer membrane, the membrane including first and second flow channels, each flow channel having upstream and downstream ends, a portion of the seawater being supplied to the first flow channel and the desalinated water being supplied to the second flow channel, the portion of the seawater serving as a source of carbon dioxide (CO2) and the desalinated water serving as a recipient of the carbon dioxide (CO2);

adding acid to the upstream end of the first flow channel to convert the bicarbonate in the portion of the seawater to carbon dioxide (CO2) in accordance with the following equation:

acid+HCO3—→CO2

passing the carbon dioxide (CO2) gas through the gas transfer membrane, whereby the carbon dioxide (CO2) gas is sequestered from the first to the second channel and is dissolved in the desalinated water.

2. The method as described in claim 1 wherein the desalination system is selected from one of the following: reverse osmosis membrane system, forward osmosis membrane system, electro dialysis system, Multi Stage Flash (MSF) system, and Multi Effect Distillation (MED) system.

3. The method as described in claim 1 wherein the desalination system is any system that produces desalinated or fresh water and concentrate waste stream from seawater.

4. The method as described in claim 1 comprising the additional step of:

adding base to the downstream end of the second flow channel, wherein the sequestered carbon dioxide (CO2) dissolved in desalinated water reacts with the added base to produce bicarbonate (HCO3—) in accordance with the following equation:

base+CO2→HCO3—+mineral

the produced bicarbonate (HCO3—) and mineral being added to the desalinated water thereby adds hardness and alkalinity to the resulting water (H2O).

5. The method as described in claim 4 wherein the added base produces bicarbonate in accordance with the following equation:

base+CO2→HCO3— and

wherein the necessary minerals are added further downstream via a separate process.

6. The method as described in claim 4 wherein a mineral is added to the downstream end of the second flow channel instead of a base, in accordance with the following equation:

mineral+CO2→HCO3—++mineral.

7. The method as described in claim 1 comprising the additional step of:

adding base to the upstream end of the second flow channel, wherein the added base reacts with the sequestered carbon dioxide (CO2) dissolved in desalinated water to produce bicarbonate (HCO3—) in accordance with the following equation:

base+CO2→HCO3—

the produced bicarbonate (HCO3—) being added to the desalinated water thereby adds hardness and alkalinity to the resulting water (H2O).

8. The method as described in claim 1 wherein the gas transfer membrane is a hydrophobic gas transferring membrane.

9. The method as described in claim 8 wherein the hydrophobic gas transferring membranes are selected from the group consisting of hollow fiber, tubular, and spiral wound types.

10. The method for remineralizing process water as described in claim 1 wherein the concentrate serves as a source of carbon dioxide (CO2), the concentrate provided to the first flow channel of the gas transfer membrane.

11. The method as described in claim 1 wherein the acid added to the upstream end of the first flow channel is selected from the group of acids consisting of: sulfuric acid (H2SO4), carbon dioxide (CO2), hydrochloric acid (HCl), and nitric acid (HNO3).

12. The method as described in claim 1 wherein the acid added to the upstream end of the first flow channel is any acid that can convert the bicarbonate in carbon dioxide (CO2) source water to carbon dioxide gas in accordance with following equation:

acid+HCO3—→CO2.

13. The method as described in claim 4 wherein the base added to the downstream end of the second flow channel is selected from the group of bases consisting of: sodium hydroxide (NaOH), potassium hydroxide (KOH), calcium hydroxide (Ca(OH)2), magnesium hydroxide (Mg(OH)2).

14. The method as described in claim 4 wherein the base added to the downstream end of the second flow channel is any base that can convert dissolved carbon dioxide (CO2) to bicarbonate (HCO3—) in accordance with the following equation:

CO2+base→HCO3—.

15. The method as described in claim 14 wherein the base is injected or added via a base filter.

16. The method as described in claim 7 wherein the base added to the upstream end of the second flow channel is selected from the group of bases consisting of sodium hydroxide (NaOH), potassium hydroxide (KOH), calcium hydroxide (Ca(OH)2), and magnesium hydroxide (Mg(OH)2).

17. The method as described in claim 7 wherein the base added to the upstream end of the second flow channel is any base that can convert dissolved carbon dioxide (CO2) to bicarbonate (HCO3—) in accordance with the following equation:

CO2+OH—→HCO3—.

18. The method as described in claim 17 wherein the base is injected or added via a base filter.

19. The method as described in claim 7 wherein the mineral added to the downstream end of the second flow channel is a calcium containing mineral.

20. The method as described in claim 6 wherein the mineral added to the downstream end of the second flow channel is selected from the group of minerals consisting of calcium oxide (CaO), calcium hydroxide (Ca(OH)2), calcium carbonate (CaCO3), calcium bicarbonate (Ca(HCO3)2), magnesium carbonate (MgCO3), magnesium oxide (MgO), and dolomite (CaMg(CO3)2).

21. A method for remineralizing process water in a seawater desalination plant, seawater used in the plant containing bicarbonate, the method comprising the following steps:

providing a desalination system including an upstream inlet for the seawater and downstream outlets for desalinated water and concentrate;

providing a gas transfer membrane, the membrane including first and second flow channels, each flow channel having upstream and downstream ends, the concentrate being supplied to the first flow channel and the desalinated water being supplied to the second flow channel, the concentrate serving as a source of carbon dioxide (CO2) and the desalinated water serving as a recipient of the carbon dioxide (CO2);

adding acid to the upstream end of the first flow channel to convert bicarbonate in the concentrate to carbon dioxide (CO2) in accordance with the following equation:

acid+HCO3—→CO2

passing the carbon dioxide (CO2) gas through the gas transfer membrane, whereby the carbon dioxide (CO2) gas is sequestered from the first to the second channel and is dissolved in the desalinated water.