IP Library Granted Patent US 12,117,239
Granted Patent B2
US 12,117,239 · App. 17/043,108 · Granted Oct 15, 2024

Liquid hydrogen production facility and hydrogen gas production facility

Inventors: Tomonori Takase (Kakogawa, JP); Shoichiro Hayashi (Kakogawa, JP); Hideki Mori (Kobe, JP)
Assignee: KAWASAKI JUKOGYO KABUSHIKI KAISHA
F25J1/001F25J1/0221C01B32/50F25J2210/42F25J2245/90
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Quick Facts
Patent No.
US 12,117,239
App. No.
17/043,108
Granted
Oct 15, 2024
Kind
B2
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.

Claims (14)

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.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 28, 2021
From: TAKASE, TOMONORI; HAYASHI, SHOICHIRO; MORI, HIDEKI
To: KAWASAKI JUKOGYO KABUSHIKI KAISHA
Reel/Frame 055060/0786 →
Priority Claims (1)
JP 2018-063762 · Mar 29, 2018 · national
Continuity (1)
Related Publication 20210025651A1 · Jan 28, 2021
Cited By (2)
US 12,473,658 US 12,476,552