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:
Nov. 07, 2023

Filed:

Apr. 24, 2019
Applicant:

Man Energy Solutions SE, Augsburg, DE;

Inventors:

Christian Schuhbauer, Hunderdorf, DE;

Dieter Verbeek, Eging am See, DE;

Rolf Bank, Deggendorf, DE;

Assignee:

MAN ENERGY SOLUTIONS SE, Augsburg, DE;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 8/06 (2006.01); B01J 8/04 (2006.01); C07C 1/04 (2006.01); C07C 1/12 (2006.01); C07C 1/02 (2006.01); C07C 9/04 (2006.01);
U.S. Cl.
CPC ...
B01J 8/067 (2013.01); B01J 8/0469 (2013.01); B01J 8/0496 (2013.01); B01J 8/065 (2013.01); C07C 1/041 (2013.01); C07C 1/042 (2013.01); C07C 1/048 (2013.01); C07C 1/12 (2013.01); B01J 2208/0053 (2013.01); B01J 2208/00539 (2013.01); B01J 2208/00548 (2013.01); B01J 2208/00663 (2013.01); B01J 2208/065 (2013.01);
Abstract

A method for carrying out catalytic gas phase reactions including providing a tube bundle reactor which has a bundle of reaction tubes that are filled with a catalyst charge and are cooled by a heat transfer medium, conveying a reaction gas through the catalyst charge, the reaction gas flowing into each reaction tube divided into two part flows introduced in the axial direction of the reaction tube at different points in the catalyst charge the catalyst charge has at least two catalyst layers of different activity, wherein the activity of the first catalyst layer, in the flow direction of the reaction gas, is lower than the activity of the at least one other catalyst layer and in step a first part flow is introduced into the first catalyst layer and each further part flow is introduced past the first catalyst layer into the at least one further catalyst layer.


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