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:
May. 26, 2026

Filed:

Mar. 31, 2022
Applicant:

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

Inventors:

Stefan Walter, Griesheim, DE;

Stephan Haase, Steinbach, DE;

Manon Cortale, Vincennes, FR;

Sophia Schmidt, Frankfurt am Main, DE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01C 1/04 (2006.01); B01D 53/14 (2006.01); B01J 19/24 (2006.01); C01B 3/36 (2026.01); C01B 3/382 (2026.01); C01B 32/40 (2017.01); C07C 29/152 (2006.01);
U.S. Cl.
CPC ...
C01C 1/0488 (2013.01); B01D 53/1475 (2013.01); B01J 19/2465 (2013.01); C01B 3/36 (2013.01); C01B 3/382 (2013.01); C01B 32/40 (2017.08); C07C 29/152 (2013.01); B01D 2252/2021 (2013.01); B01J 2219/00186 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/025 (2013.01); C01B 2203/0415 (2013.01); C01B 2203/042 (2013.01); C01B 2203/061 (2013.01); C01B 2203/068 (2013.01); C01B 2203/0811 (2013.01); C01B 2203/1241 (2013.01); C01B 2203/148 (2013.01);
Abstract

What is proposed is a process and a plant for parallel production of methanol and ammonia by heterogeneously catalyzed reaction of hydrogen and carbon oxides on the one hand and hydrogen and nitrogen on the other hand. This includes producing a raw synthesis gas stream and dividing it into two portions. A first raw synthesis gas substream is used as input for a methanol synthesis to obtain raw methanol and a methanol synthesis purge stream. A second raw synthesis gas substream is subjected to a CO conversion, a carbon dioxide separation and a liquid nitrogen scrubbing and then sent to an ammonia synthesis. According to the invention at least a portion of the methanol synthesis purge stream is sent to the ammonia synthesis and at least one substream obtained from the second raw synthesis gas substream is passed to the methanol synthesis.


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