Capacitive deionization process

Patent metadata

Field	Value
Publication number	US-12110240-B2
Application number	US-202117534301-A
Country	US
Kind code	B2
Filing date	Nov 23, 2021
Priority date	Apr 29, 2021
Publication date	Oct 8, 2024
Grant date	Oct 8, 2024

Abstract

A capacitive deionization process is provided. The capacitive deionization process includes a charging step of applying power to a capacitive deionization apparatus in a charging state and supplying charge water containing target dissolved ions to be precipitated to the capacitive deionization apparatus for a predetermined period of time, a discharging step of applying power to the capacitive deionization apparatus in a discharging state and supplying discharge water in which the target dissolved ions are in a saturated state to the capacitive deionization apparatus for a predetermined period of time, and a crystal recovery step of recovering a crystal of the target dissolved ions precipitated in the capacitive deionization apparatus and/or the discharge water.

First claim

What is claimed is:

1. A capacitive deionization process comprising:
a charge water providing step of providing charge water containing lithium ions and other impurities by first heat-treating nickel-cobalt-manganese-lithium mixture of a waste battery and then dissolving the heat-treated nickel-cobalt-manganese-lithium mixture of the waste battery;
a discharge water providing step of providing discharge water containing lithium ions and ethanol such that lithium ions are in a saturated state in the discharge water, wherein a ratio of the ethanol in the total discharge water is maintained at a substantially constant 50%;
a charging step of applying power to a capacitive deionization apparatus in a charging state and supplying the charge water to the capacitive deionization apparatus for a first predetermined period of time;
a charge water removing step of removing, after the first predetermined period of time, the charge water from the capacitive deionization apparatus, wherein the capacitive deionization apparatus remains in the charging state until complete removal of the charge water from the capacitive deionization apparatus;
a discharging step of applying power to the capacitive deionization apparatus in a discharging state and supplying the discharge water to the capacitive deionization apparatus for a second predetermined period of time; and
a discharge water removing step of removing, after the second predetermined period of time, the discharge water from the capacitive deionization apparatus,
a crystal recovery step of recovering a crystal of the lithium ions precipitated in the capacitive deionization apparatus and/or the discharge water, wherein the crystal recovery step is performed after repeating the charging step, the charge water removing step, the discharging step, the discharge water removing step for a third predetermined period of time.

2. The capacitive deionization process according to claim 1 , wherein in the discharging step, the discharge water contains the lithium ions at a high concentration equal to or higher than a saturation concentration.

3. The capacitive deionization process according to claim 2 , wherein the concentration of the lithium ions in the discharge water is increased by repeating the charging and discharging steps.

4. The capacitive deionization process according to claim 2 , wherein the discharge water contains the lithium ions by dissolving a salt of the lithium hydroxide in the discharge water.

5. The capacitive deionization process according to claim 1 , wherein the charge water is purified through the charging step.

6. The capacitive deionization process according to claim 1 , wherein the capacitive deionization apparatus is a batch type apparatus.

7. The capacitive deionization process according to claim 6 , wherein the capacitive deionization apparatus is connected to a charge water tank containing the charge water and a discharge water tank containing the discharge water.

8. The capacitive deionization process according to claim 7 , wherein the discharge water accommodated in the discharge water tank is circulated through the capacitive deionization apparatus.

9. The capacitive deionization process according to claim 1 , wherein the discharging step is performed after the charge water in the capacitive deionization apparatus is completely removed from the capacitive deionization apparatus in the charging step.

10. The capacitive deionization process according to claim 1 , wherein the discharging step is performed after the charge water in the capacitive deionization apparatus is completely removed from the capacitive deionization apparatus in the charging step.

11. The capacitive deionization process according to claim 10 , wherein the charging step is performed after the discharge water in the capacitive deionization apparatus is completely removed from the capacitive deionization apparatus in the discharging step.

12. The capacitive deionization process of claim 1 , wherein the charge water providing step comprises: adding lithium carbonate into the charge water and then adding barium hydroxide into the charge water to convert lithium carbonate into lithium hydroxide.

Assignees

• Doosan Enerbility Co Ltd

Inventors

• Kang Wee Kwan
• Jo Ho Yong
• You Jang Yong

Classifications

• C02F2001/5218

  Crystallization · CPC title

• C01D15/02

  Oxides; Hydroxides · CPC title

• C02F2101/10

  Inorganic compounds · CPC title

• C01P2002/72

  by d-values or two theta-values, e.g. as X-ray diagram · CPC title

• C01D15/08

  Carbonates; Bicarbonates · CPC title