Liquid hydrogen production facility and hydrogen gas production facility

Patent metadata

Field	Value
Publication number	US-12117239-B2
Application number	US-201917043108-A
Country	US
Kind code	B2
Filing date	Mar 27, 2019
Priority date	Mar 29, 2018
Publication date	Oct 15, 2024
Grant date	Oct 15, 2024

Abstract

A reformer configured to generate hydrogen gas by reforming a hydrocarbon; a hydrogen liquefier configured to generate liquid hydrogen by liquefying the hydrogen gas; a reservoir for storing the liquid hydrogen; and a heat exchanger configured to cause heat exchange between boil-off gas that occurs in the reservoir and carbon dioxide that occurs during a process of generating the hydrogen gas to liquefy the carbon dioxide.

First claim

The invention claimed is:

1. A liquid hydrogen production facility comprising:
a reformer configured to generate hydrogen gas by reforming a hydrocarbon, the reformer outputting the hydrogen gas to a hydrogen liquefier and carbon dioxide to a heat exchanger;
a reservoir;
the hydrogen liquefier, the hydrogen liquefier being configured to generate liquid hydrogen by liquefying the hydrogen gas received from the reformer, the hydrogen liquefier outputting the liquid hydrogen to the reservoir for storage; and
the heat exchanger, the heat exchanger being configured to receive boil-off gas from the liquid hydrogen in the reservoir and the carbon dioxide from the reformer and cause heat exchange between the boil-off gas and the carbon dioxide to liquefy the carbon dioxide.

2. The liquid hydrogen production facility according to claim 1 , wherein the hydrocarbon is methane.

3. The liquid hydrogen production facility according to claim 2 , wherein the reformer reforms the hydrocarbon by steam reforming.

4. The liquid hydrogen production facility according to claim 1 , wherein the reformer reforms the hydrocarbon by steam reforming.

5. A liquid hydrogen production facility comprising:
a reformer configured to generate hydrogen gas by reforming a hydrocarbon, the reformer outputting the hydrogen gas to a hydrogen liquefier and carbon dioxide to a heat exchanger;
a hydrogen liquefier configured to receive liquid nitrogen and generate liquid hydrogen by liquefying the hydrogen gas received from the reformer, by cooling the hydrogen gas with use of heat of vaporization of the liquid nitrogen, the hydrogen liquefier outputting nitrogen gas to the heat exchanger; and
the heat exchanger, the heat exchanger being configured to receive the nitrogen gas from the hydrogen liquefier and cause heat exchange between the nitrogen gas and the carbon dioxide to liquefy the carbon dioxide.

6. The liquid hydrogen production facility according to claim 5 , wherein the hydrocarbon is methane.

7. The liquid hydrogen production facility according to claim 5 , wherein the reformer reforms the hydrocarbon by steam reforming.

Assignees

• Kawasaki Heavy Ind Ltd

Inventors

• Takase Tomonori
• Hayashi Shoichiro
• Mori Hideki

Classifications

• F25J2245/90

  the recycled stream being boil-off gas from storage · CPC title

• F25J2210/42

  Nitrogen · CPC title

• F25J1/0221

  using the cold stored in an external cryogenic component in an open refrigeration loop · CPC title

• C01B32/50

  Carbon dioxide · CPC title

• Y02E60/32

  Hydrogen storage · CPC title