Method for preparing hydrogen gas

Patent metadata

Field	Value
Publication number	US-12275639-B2
Application number	US-202217874248-A
Country	US
Kind code	B2
Filing date	Jul 26, 2022
Priority date	Mar 8, 2022
Publication date	Apr 15, 2025
Grant date	Apr 15, 2025

Abstract

A method for preparing hydrogen gas includes a decomposition step, a first adsorption step, a second adsorption step, a first regeneration step, a third heat-exchange step, and a second regeneration step.

First claim

What is claimed is:

1. A method for preparing hydrogen gas, the method comprising:
a decomposition step of decomposing ammonia-containing gas to produce decomposition-product gas, which contains nitrogen (N 2 ), hydrogen (H 2 ), and undecomposed ammonia, and exhaust gas;
a first adsorption step of adsorbing and removing the undecomposed ammonia contained in the decomposition-product gas by a first adsorbent to produce first product gas containing nitrogen (N 2 ) and hydrogen (H 2 );
a second adsorption step of adsorbing and removing the nitrogen (N 2 ) contained in the first product gas by a second adsorbent to produce higher-purity hydrogen (H 2 );
a first regeneration step of regenerating the second adsorbent by desorbing the nitrogen (N 2 ) adsorbed to the second adsorbent while generating second off gas containing nitrogen (N 2 ) and hydrogen (H 2 ); and
a third heat-exchange step of heat-exchanging the exhaust gas transferred from the decomposition step and at least a portion of the second off gas transferred from the first regeneration step; and
a second regeneration step of regenerating the first adsorbent after the first adsorption step by transferring, to the first adsorbent, the exhaust gas and the at least a portion of the second off gas, which are heat-exchanged in the third heat-exchange step and serve as heating-desorbing gas, and a remainder of the second off gas, which is transferred from the first regeneration step and serves as cooling-cleaning gas.

2. The method of claim 1 , wherein the exhaust gas transferred from the decomposition step has a temperature in a range of 500° C. to 800° C., and
wherein the second off gas transferred from the first regeneration step has a temperature of 20° C. to 50° C.

3. The method of claim 1 , wherein the first adsorption step is performed through a thermal swing adsorption (TSA) manner.

4. The method of claim 1 , wherein the second adsorption step is performed through a pressure swing adsorption (PSA) manner.

5. The method of claim 1 , wherein the second off gas heat-exchanged in the third heat-exchange step has a temperature in a range of 400° C. or more and less than 600° C., and
wherein the exhaust gas heat-exchanged in the third heat-exchange step has a temperature in a range of 500° C. or more and less than 650° C.

6. The method of claim 1 , wherein the second regeneration step further includes:
additionally heat-exchanging the exhaust gas heat-exchanged in the third heat-exchange step with the first adsorbent to increase an ambient temperature of the first adsorbent.

7. The method of claim 6 , wherein the second regeneration step further includes:
passing the at least a portion of the second off gas heat-exchanged in the third heat-exchange step through an adsorption bed while directly making contact with the first adsorbent, and
heat-exchanging the exhaust gas heat-exchanged in the third heat-exchange step with the first adsorbent without directly making contact with the first adsorbent.

8. The method of claim 1 , wherein the first adsorbent is filled in a plurality of adsorption beds.

9. The method of claim 8 , wherein a number of the plurality of adsorption beds filled with the first adsorbent is three.

10. The method of claim 8 , wherein a number of the plurality of adsorption beds, which are filled with the first adsorbent, is 2n+2, and wherein, “n” is a natural number.

11. The method of claim 8 , further comprising:
passing the at least a portion of the second off gas, which is heat-exchanged in the third heat-exchange step, through at least one of the plurality of adsorption beds, and
passing the exhaust gas heat-exchanged in the third heat-exchange step through a flow path for the exhaust gas.

12. The method of claim 1 , further comprising:
a nitrogen oxide removing step of discharging the exhaust gas transferred from the second regeneration step, after a nitrogen oxide is removed.

13. The method of claim 1 , wherein the first adsorbent includes at least one of a carbon-based material and a zeolite-based material.

14. The method of claim 8 , further comprising repeating a cycle in each of the plurality of adsorption beds in the first adsorption step and the second regeneration step independently, the cycle sequentially includes:
an adsorbing process of adsorbing the undecomposed ammonia to the first adsorbent while supplying the decomposition-product gas, which is transferred from the decomposition step, to each of the plurality of adsorption beds;
a desorbing process of desorbing the adsorbed ammonia by allowing the at least a portion of the second off gas, which is heat-exchanged in the third heat-exchange step, to pass through each of the plurality of adsorption beds; and
a cleaning process of cleaning the first adsorbent by allowing the remaining second off gas transferred from the second adsorption step to pass through each of the plurality of adsorption beds.

15. The method of claim 14 , wherein the plurality of adsorption beds in the first adsorption step and the second regeneration step include at least three adsorption beds individually performing the adsorbing process, the desorbing process, and the cleaning process, and alternately performing the cycle in sequence of the adsorbing process, the desorbing process, and the cleaning process.

16. The method of claim 1 , wherein the second regeneration step further includes: generating first off gas including undecomposed ammonia, which is adsorbed to the first adsorbent and serves as a by-product, nitrogen (N 2 ), and hydrogen (H 2 ), and
recirculating the first off gas to the decomposition step.

17. The method of claim 1 , further comprising:
a first heat-exchange step of generating ammonia in a gas phase by heat-exchanging ammonia in a liquid phase with the decomposition-product gas, which is transferred from the decomposition step to the first adsorption step;
a second heat-exchange step of increasing a temperature of the ammonia in the gas phase by heat-exchanging the ammonia in the gas phase with the exhaust gas transferred from the decomposition step; and
introducing the ammonia heat-exchanged in the second heat-exchange step into the decomposition step.

Assignees

• Hyundai Motor Co Ltd
• Kia Corp

Inventors

• Shin Byeong Soo
• Lee Kyung Moon
• Cho Young Jin
• Park Yong Ha
• Park Hoon Mo
• Nam Dong Hoon

Classifications

• B01D2253/108

  Zeolites · CPC title

• C01B2203/08

  Methods of heating or cooling · CPC title

• C01B2203/042

  Purification by adsorption on solids · CPC title

• C01B2203/0277

  containing a catalytic decomposition step · CPC title

• B01D2257/404

  Nitrogen oxides other than dinitrogen oxide · CPC title