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:
Sep. 02, 2008

Filed:

Apr. 06, 2004
Applicants:

Andrzej M. Malek, Doylestown, PA (US);

Stephen C. Leviness, Tulsa, OK (US);

Horacio M. Trevino, Annandale, NJ (US);

Weldon K. Bell, Ridgeway, IA (US);

David O. Marler, Morris Plains, NJ (US);

Inventors:

Andrzej M. Malek, Doylestown, PA (US);

Stephen C. Leviness, Tulsa, OK (US);

Horacio M. Trevino, Annandale, NJ (US);

Weldon K. Bell, Ridgeway, IA (US);

David O. Marler, Morris Plains, NJ (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 23/00 (2006.01); B01J 21/00 (2006.01); B01J 20/00 (2006.01); B01J 27/00 (2006.01); B01J 29/00 (2006.01);
U.S. Cl.
CPC ...
Abstract

A process for enhancing the activity of a catalyst metal particulate for hydrogenation reactions comprising calcining the particulate in an oxidant-containing atmosphere to partially oxidize it thereby forming a porous layer of oxides thereon, treating with an solution capable of oxidizing the calcined metal particulate and comprising a compound of a hydrogenation catalyst metal to where said metal particulate has absorbed a volume of solution equal to at least about 10% of its calculated pore volume and activating it by treatment with a hydrogen-containing gas at elevated temperatures thereby forming a dispersed active metal catalyst. Preferably, the treated particulate is calcined a second time under the same conditions as the first before final activation with a hydrogen-containing gas. The metal particulate is preferably sized after each calcination and any agglomerates larger than 250 microns are comminuted to a desired size.


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