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:
Jan. 07, 2025

Filed:

May. 04, 2022
Applicant:

L'air Liquide Société Anonyme Pour I'etude ET I'exploitation Des Procédés Georges Claude, Paris, FR;

Inventors:

Bertrand Demolliens, Paris, FR;

Antoine Hernandez, Saint Maur des Fossés, FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
F25J 3/08 (2006.01); B01D 53/00 (2006.01); B01D 53/047 (2006.01); C01B 3/50 (2006.01); C01B 3/56 (2006.01); C01B 32/40 (2017.01); F25J 3/06 (2006.01);
U.S. Cl.
CPC ...
C01B 3/506 (2013.01); B01D 53/002 (2013.01); B01D 53/047 (2013.01); C01B 3/56 (2013.01); C01B 32/40 (2017.08); F25J 3/0675 (2013.01); B01D 2256/16 (2013.01); B01D 2257/502 (2013.01); B01D 2257/504 (2013.01); B01D 2257/80 (2013.01); C01B 2203/042 (2013.01); C01B 2203/046 (2013.01); C01B 2203/047 (2013.01);
Abstract

In a process for the separation of a mixture containing hydrogen and carbon monoxide to produce gaseous hydrogen, the mixture is cooled down to a temperature below −180° C. and then separated at a temperature below −100° C. to produce a gas enriched in hydrogen and a fluid enriched in carbon monoxide, at least a part of the gas enriched in hydrogen is sent to a pressure swing adsorption separation apparatus operating at a temperature above 0° C. to produce a gas rich in hydrogen at a pressure of at least 20 bars, and at least a part of the gas rich in hydrogen is cooled in the heat exchanger down to a temperature below −100° C., reduced in pressure in a turbine down to a pressure of at least 8 bars and reheated in the heat exchanger to constitute a product rich in hydrogen at a pressure of at least 8 bars.


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