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:

Sep. 19, 2019
Applicant:

Basf SE, Ludwigshafen am Rhein, DE;

Inventors:

Andrey Karpov, Ludwigshafen am Rhein, DE;

Marco Oskar Kennema, Ludwigshafen am Rhein, DE;

Nicolas Duyckaerts, Ludwigshafen am Rhein, DE;

Christian Walsdorff, Ludwigshafen am Rhein, DE;

Christian Bartosch, Ludwigshafen am Rhein, DE;

Juergen Zuehlke, Ludwigshafen am Rhein, DE;

Miguel Angel Romero Valle, Ludwigshafen am Rhein, DE;

Assignee:

BASF SE, Ludwigshafen am Rhein, DE;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07D 301/10 (2006.01); B01J 21/04 (2006.01); B01J 23/68 (2006.01); B01J 35/31 (2024.01); B01J 35/40 (2024.01); B01J 35/56 (2024.01); B01J 35/61 (2024.01); B01J 35/63 (2024.01); B01J 35/66 (2024.01);
U.S. Cl.
CPC ...
C07D 301/10 (2013.01); B01J 21/04 (2013.01); B01J 23/688 (2013.01); B01J 35/31 (2024.01); B01J 35/40 (2024.01); B01J 35/56 (2024.01); B01J 35/612 (2024.01); B01J 35/633 (2024.01); B01J 35/695 (2024.01);
Abstract

A process for producing ethylene oxide by gas-phase oxidation of ethylene, comprising: directing a feed comprising gaseous ethylene and gaseous oxygen through a packing of individual shaped catalyst bodies, under conditions conducive to obtain a reaction mixture containing at least 2.7 vol.-% of ethylene oxide, wherein each shaped catalyst body comprises silver deposited on a refractory support and is characterized by a content of at least 20 wt.-% of silver, relative to the total weight of the shaped catalyst body; a BET surface area in the range of 1.6 to 3.0 m/g; a first face side surface, a second face side surface and a circumferential surface with a plurality of passageways extending from the first face side surface to the second face side surface; and a uniform multilobed cross-section; and a longest direct diffusion pathway d, with 2being in the range of 0.7 to 2.4 mm, wherein the longest diffusion pathway d is defined as the shortest distance from the geometric surface of the shaped catalyst body to a point inside the structure of the shaped catalyst body for which point the shortest distance is the largest among all points. The process allows for increased activity and/or stability of the catalyst while maintaining or increasing selectivity at high productivity.


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