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:
Apr. 18, 2023

Filed:

Dec. 13, 2021
Applicant:

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

Inventors:

Veronika Gronemann, Karben, DE;

Karin Huder, Frankfurt am Main, DE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 29/151 (2006.01); B01D 53/047 (2006.01); B01J 19/24 (2006.01); C01B 3/24 (2006.01); C01B 3/36 (2006.01); C01B 3/56 (2006.01);
U.S. Cl.
CPC ...
C07C 29/1518 (2013.01); B01D 53/047 (2013.01); B01J 19/245 (2013.01); C01B 3/24 (2013.01); C01B 3/36 (2013.01); C01B 3/56 (2013.01); B01J 2219/0004 (2013.01); C01B 2203/0216 (2013.01); C01B 2203/0255 (2013.01); C01B 2203/0272 (2013.01); C01B 2203/0405 (2013.01); C01B 2203/061 (2013.01); C01B 2203/1241 (2013.01);
Abstract

Proposed is a process for producing methanol from synthesis gas by means of multi-stage, for example two-stage, heterogeneously catalyzed methanol synthesis, wherein the methanol product formed in every synthesis stage is separated by condensation and the remaining residual gas is supplied to the downstream synthesis stage or after separation of a purge stream recycled to the first synthesis stage as a recycle stream. According to the invention after each synthesis stage the residual gas streams have separated from them a respective purge stream, from which, using one or more hydrogen recovery apparatuses, hydrogen is separated and recycled to the first synthesis stage. The ratio of the individual purge streams and their total molar flow may optionally be varied to allow better control of the reaction in the individual synthesis stages and to allow reaction to the advancing deactivation of the catalysts present therein.


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