Hydrogen purification/storage apparatus and method using liquid organic hydrogen carrier

Patent metadata

Field	Value
Publication number	US-12134559-B2
Application number	US-202017101140-A
Country	US
Kind code	B2
Filing date	Nov 23, 2020
Priority date	Dec 19, 2019
Publication date	Nov 5, 2024
Grant date	Nov 5, 2024

Abstract

The present disclosure relates to a hydrogen purification/storage apparatus and method using a liquid organic hydrogen carrier (LOHC).

First claim

What is claimed is:

1. A hydrogen purification and storage apparatus comprising:
a hydrogen supply unit;
a reaction unit connected to the hydrogen supply unit via a hydrogen supply line, the reaction unit comprising a hydrogen storage material and a catalyst configured to accelerate hydrogenation of the hydrogen storage material; and
a compressor installed in the hydrogen supply line, the compressor being configured to compress hydrogen supplied from the hydrogen supply unit, wherein
the hydrogen storage material comprises a liquid organic hydrogen carrier (LOHC);
wherein the hydrogen supply line comprises:
a first hydrogen supply line configured to interconnect the hydrogen supply unit and the compressor;
a second hydrogen supply line configured to interconnect the compressor and the reaction unit; and
a third hydrogen supply line configured to interconnect the compressor and the reaction unit along a path different from a path of the second hydrogen supply line, the third hydrogen supply line having a buffer tank.

2. The hydrogen purification and storage apparatus according to claim 1 , wherein the hydrogen supply unit supplies pure hydrogen or a mixed gas comprising hydrogen and an impurity selected from a group consisting of nitrogen (N 2 ), carbon oxide, hydrocarbon, oxygen (O 2 ), and a combination thereof.

3. The hydrogen purification and storage apparatus according to claim 1 , further comprising no purification unit.

4. The hydrogen purification and storage apparatus according to claim 1 , wherein the hydrogen supply line further comprises a bypass line configured to interconnect the first hydrogen supply line and the second hydrogen supply line, the bypass line being configured to bypass the compressor.

5. The hydrogen purification and storage apparatus according to claim 1 , wherein, when pressure of hydrogen supplied from the hydrogen supply unit is equal to or higher than a predetermined pressure value, a valve installed in each of the first hydrogen supply line and the second hydrogen supply line is opened such that the hydrogen is supplied to the first hydrogen supply line and the second hydrogen supply line.

6. The hydrogen purification and storage apparatus according to claim 1 , wherein, when pressure of hydrogen supplied from the hydrogen supply unit is lower than a predetermined pressure value, the compressor compresses the hydrogen and supplies the compressed hydrogen, and a valve installed in each of the first hydrogen supply line and the third hydrogen supply line is opened such that the compressed hydrogen is supplied to the first hydrogen supply line and the third hydrogen supply line.

7. The hydrogen purification and storage apparatus according to claim 1 , wherein the liquid organic hydrogen carrier (LOHC) comprises any one selected from a group consisting of biphenyl dissolved in diphenylmethane, N-ethylcarbazole, dibenzyl toluene, toluene, and a combination thereof.

8. The hydrogen purification and storage apparatus according to claim 1 , wherein the catalyst comprises a catalyst metal selected from a group consisting of ruthenium (Ru), nickel (Ni), palladium (Pd), platinum (Pt), and a combination thereof.

9. The hydrogen purification and storage apparatus according to claim 1 , wherein the reaction unit is operated at a temperature of 20° C. to 150° C. and a pressure of 10 bar to 50 bar.

10. The hydrogen purification and storage apparatus according to claim 1 , wherein a reaction between the hydrogen storage material and the hydrogen in the reaction unit is performed in a closed system.

11. The hydrogen purification and storage apparatus according to claim 1 , further comprising a pressure measurement unit installed at the reaction unit, the pressure measurement unit being configured to measure pressure of the reaction unit.

12. The hydrogen purification and storage apparatus according to claim 1 , further comprising a storage unit connected to the reaction unit, the storage unit being configured to store a product in the reaction unit.

13. The hydrogen purification and storage apparatus according to claim 1 , further comprising a hydrogen storage material supply unit connected to the reaction unit, the hydrogen storage material supply unit being configured to supply the hydrogen storage material to the reaction unit.

14. The hydrogen purification and storage apparatus according to claim 1 , further comprising:
a purge gas supply unit communicating with the second hydrogen supply line, the purge gas supply unit being configured to supply a purge gas to the reaction unit, wherein
residual gas in the reaction unit is discharged outside via the third hydrogen supply line and a purge gas discharge line communicating therewith by the purge gas.

15. A hydrogen purification and storage method using the hydrogen purification and storage apparatus according to claim 1 , wherein the hydrogen purification and storage method comprises reacting hydrogen supplied from the hydrogen supply unit to the reaction unit and the hydrogen storage material in the reaction unit with each other.

16. The hydrogen purification and storage method according to claim 15 , wherein
a reaction between the hydrogen storage material and the hydrogen in the reaction unit is performed in a closed system, and
when pressure in the reaction unit reaches a predetermined value, the reaction unit is opened to move a product in the reaction unit to a storage unit connected to the reaction unit.

17. The hydrogen purification and storage method according to claim 16 , wherein a new hydrogen storage material is supplied to the reaction unit after the product in the reaction unit is moved to the storage unit.

18. The hydrogen purification and storage method according to claim 15 , wherein, when pressure of hydrogen supplied from the hydrogen supply unit is equal to or higher than a predetermined pressure value, the hydrogen is supplied to the first hydrogen supply line and the second hydrogen supply line.

19. The hydrogen purification and storage method according to claim 16 , wherein,
when pressure of hydrogen supplied from the hydrogen supply unit is lower than a predetermined pressure value, the hydrogen is compressed and supplied to the first hydrogen supply line and the third hydrogen supply line.

20. The hydrogen purification and storage method according to claim 15 , further comprising injecting a purge gas into the reaction unit to discharge residual gas in the reaction unit to an outside before supplying hydrogen to the hydrogen supply unit.

Assignees

• Korea Inst Sci & Tech

Inventors

• Jo Young Suk
• Park Yong Ha
• Kim Yeong Cheon
• Jeong Hyang Soo
• Kim Yong Min
• Sohn Hyun Tae
• Yoon Chang Won
• Nam Suk Woo
• Han Jong Hee

Classifications

• B01J2208/00548

  Flow · CPC title

• C01B2203/1064

  Platinum group metal catalysts · CPC title

• C01B2203/1058

  Nickel catalysts · CPC title

• C01B2203/0435

  Catalytic purification · CPC title

• C01B2203/1633

  Measuring the pressure · CPC title