System and method for treating brine and capturing CO2 emissions

Patent metadata

Field	Value
Publication number	US-12187629-B2
Application number	US-202318201391-A
Country	US
Kind code	B2
Filing date	May 24, 2023
Priority date	May 24, 2023
Publication date	Jan 7, 2025
Grant date	Jan 7, 2025

Abstract

A system of treating reject brine and capturing carbon dioxide (CO2) includes a two-stage electrodialysis (ED) process for producing multiple products with high purity from rejected brine and flue gas mixtures (10% CO2 and 90% N2) emitted from an industrial plant. According to an embodiment, the system includes a first electrodialysis (ED) stage and a second electrodialysis (ED) stage in series.

First claim

The invention claimed is:

1. A system for treating reject brine and capturing carbon dioxide (CO 2 ) from an industrial plant, comprising:
a first electrodialysis (ED) stage including:
a plurality of cell pairs defined between cation exchange membranes, each of the cell pairs including a multivalent ion chamber and a monovalent ion chamber, the multivalent ion chamber and the monovalent ion chamber being separated by an anion exchange membrane;
a first cathode and a first anode at respective ends of the plurality of cell pairs;
a first anolyte chamber defined between the first anode and an adjacent cation exchange membrane; and
a first catholyte chamber defined between the first cathode and an adjacent cation exchange membrane;

a second electrodialysis (ED) stage including:
a plurality of cell groups defined between bipolar membranes, each of the cell groups including a flue gas chamber, a carbonate chamber adjacent the flue gas chamber, a concentrated brine chamber adjacent the carbonate chamber, and an acid chamber adjacent the concentrated brine chamber, the flue gas chamber and the carbonate chamber being separated by an anion exchange membrane, the carbonate chamber and the concentrated brine chamber being separated by a cation exchange membrane, the concentrated brine chamber and the acid chamber being separated by an anion exchange membrane;
a second cathode and a second anode at respective ends of the plurality of cell groups;
a second anolyte chamber defined between the second anode and an adjacent semi-permeable membrane;
a second catholyte chamber defined between the second cathode and an adjacent semi-permeable membrane; and
a bubble column contactor connected to the flue gas chamber; and

a freeze-dryer.

2. The system as recited in claim 1 , wherein the industrial plant is a desalination plant.

3. The system of claim 1 , wherein the first ED stage includes a first electrolyte in the first anolyte and catholyte chambers and the second ED stage includes a first electrolyte in the second anolyte chamber and a second electrolyte in the second catholyte chamber.

4. The system of claim 1 , wherein the first electrolyte in the first ED stage includes sulphamic acid, the first electrolyte in the second ED stage includes sulphamic acid, and the second electrolyte in the second ED stage includes sodium hydroxide.

5. A method of desalinating reject brine and flue gas emitted from an industrial plant using the system of claim 1 , comprising:
providing reject brine from an industrial plant to the multivalent ion chamber;
providing water to the monovalent ion chamber;
transporting NaCl and monovalent ions through the anion exchange membrane to provide a concentrated brine and monovalent ion mixture;
collecting a stream of water with multivalent ions from the multivalent ion chamber;
transferring the concentrated reject brine and monovalent ion mixture to the concentrated brine chamber of the second ED stage;
dissolving CO 2 emissions from the industrial plant to provide a flue gas mixture including provide CO 3 −2 and HCO 3 −1 ions;
transferring the flue gas mixture including CO 3 −2 and HCO 3 −1 ions to the flue gas chamber of the second ED stage;
transporting the CO 3 −2 and HCO 3 −1 ions from the flue gas chamber to the carbonates chamber through the anion exchange membrane;
providing water to the acid chamber;
transporting sodium ions from the concentrated brine chamber through the cation exchange membrane to the carbonate chamber to produce a sodium carbonate mixture; and
transporting chloride ions from the concentrated brine chamber to the acid chamber through the anion exchange membrane to produce an acid mixture.

6. The method of claim 5 , wherein the acid mixture includes HCl and H 2 SO 4 .

7. The method of claim 6 , wherein the acid mixture includes more than about 90% HCl.

8. The method of claim 5 , wherein an electrolyte is circulated between the first catholyte and anolyte chambers of the first ED stage.

9. The method of claim 8 , wherein the electrolyte is sulphamic acid.

10. The method of claim 5 , wherein an electrolyte is separately circulated in each of the second anolyte and second catholyte chambers of the second ED stage.

11. The method of claim 10 , wherein the electrolyte circulated in the second anolyte chamber is sulphamic acid.

12. The method of claim 11 , wherein the electrolyte circulated in the second catholyte chamber is sodium hydroxide.

Assignees

• Univ United Arab Emirates

Inventors

• Mustafa Jawad
• Al-Marzouqi Ali H
• Ghasem Nayef Mohamed

Classifications

• C02F1/265 Primary

  Desalination · CPC title

• C02F1/66

  by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title

• C02F2103/08

  Seawater, e.g. for desalination · CPC title

• C02F1/4693 Primary

  electrodialysis · CPC title

• Y02C20/40

  of CO2 · CPC title