The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Mar. 24, 2026

Filed:

Dec. 16, 2022
Applicant:

L'air Liquide, Societe Anonyme Pour L'etude ET L'exploitation Des Procedes Georges Claude, Paris, FR;

Inventors:

Michael A. Turney, Houston, TX (US);

Alain Guillard, Houston, TX (US);

Bobby Chan, Houston, TX (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
F25J 1/02 (2006.01); C01B 3/506 (2026.01); C09K 5/04 (2006.01); F25J 1/00 (2006.01);
U.S. Cl.
CPC ...
F25J 1/0234 (2013.01); C01B 3/506 (2013.01); C09K 5/041 (2013.01); F25J 1/001 (2013.01); F25J 1/0072 (2013.01); F25J 1/0075 (2013.01); F25J 1/0205 (2013.01); F25J 1/0237 (2013.01); F25J 1/0254 (2013.01); C01B 2210/0009 (2013.01); C01B 2210/0048 (2013.01); C09K 2205/132 (2013.01); F25J 2210/40 (2013.01); F25J 2210/42 (2013.01); F25J 2210/62 (2013.01); F25J 2215/10 (2013.01); F25J 2245/42 (2013.01); F25J 2270/12 (2013.01); F25J 2270/14 (2013.01); F25J 2290/12 (2013.01);
Abstract

An integrated industrial unit is provided, which can include: a nitrogen source comprising an air separation unit that is configured to provide pressurized gaseous nitrogen and liquid nitrogen; a hydrogen source; a hydrogen liquefaction unit, wherein the hydrogen liquefaction unit comprises a precooling system, and a liquefaction system; and a liquid hydrogen storage tank, wherein the precooling system is configured to receive the gaseous hydrogen from the hydrogen source and cool the gaseous hydrogen to a temperature between 70K and 100K, wherein the precooling system comprises a primary refrigeration system and a secondary refrigeration system, wherein the liquefaction system is in fluid communication with the precooling system and is configured to liquefy the gaseous hydrogen received from the precooling system to produce liquid hydrogen, wherein the liquid hydrogen storage tank is in fluid communication with the liquefaction system and is configured to store the liquid hydrogen received from the liquefaction system.


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