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. 26, 2021

Filed:

Apr. 26, 2018
Applicant:

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

Inventors:

Frank Castillo-Welter, Friedrichsdorf, DE;

Stephane Haag, Frankfurt am Main, DE;

Robert Frind, Kreischa, DE;

Timm Schuhmann, Offenbach, DE;

Andreas Ochs, Bad Homburg, DE;

Marc Wagner, Saint Maur des Fosses, FR;

Solene Valentin, Le Pecq, FR;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 8/04 (2006.01); C07C 29/152 (2006.01); B01J 8/06 (2006.01); C07C 31/04 (2006.01);
U.S. Cl.
CPC ...
B01J 8/0496 (2013.01); B01J 8/0415 (2013.01); B01J 8/0438 (2013.01); B01J 8/0453 (2013.01); B01J 8/067 (2013.01); C07C 29/152 (2013.01); B01J 2208/00141 (2013.01); B01J 2208/00176 (2013.01); B01J 2208/025 (2013.01); B01J 2219/0002 (2013.01); B01J 2219/0004 (2013.01); C07C 31/04 (2013.01);
Abstract

A reactor for conducting exothermic equilibrium reactions, especially for the performance of methanol synthesis by heterogeneously catalysed conversion of synthesis gas, is proposed, which enables readjustment and hence optimization of the reaction conditions along the longitudinal coordinate of the reactor. For this purpose, in accordance with the invention, the reactor is divided into a multitude of series-connected reaction cells, each of which comprises a preheating zone, a cooled reaction zone, one or more cooling zones and a deposition zone for condensable reaction products. In this way, the reaction conditions are adjustable to the respective, local composition of the reaction mixture and variable over the reactor length.


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