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:
Jul. 12, 2016

Filed:

May. 10, 2010
Applicants:

Massimo Iovane, San Donato Milanese, IT;

Roberto Zennaro, Milan, IT;

Pio Forzatti, Monza, IT;

Gianpiero Groppi, Segrate, IT;

Luca Lietti, Cantu, IT;

Enrico Tronconi, Arcore, IT;

Carlo Giorgio Visconti, Basiglio, IT;

Stefano Rossini, Milan, IT;

Elsa Mignone, Monza, IT;

Inventors:

Massimo Iovane, San Donato Milanese, IT;

Roberto Zennaro, Milan, IT;

Pio Forzatti, Monza, IT;

Gianpiero Groppi, Segrate, IT;

Luca Lietti, Cantu, IT;

Enrico Tronconi, Arcore, IT;

Carlo Giorgio Visconti, Basiglio, IT;

Stefano Rossini, Milan, IT;

Elsa Mignone, Monza, IT;

Assignee:

ENI S.p.A., Rome, IT;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01J 8/00 (2006.01); B01J 8/02 (2006.01); B01J 19/00 (2006.01); B01J 19/24 (2006.01); B01J 19/30 (2006.01); B01J 19/32 (2006.01); C10G 2/00 (2006.01); B01J 8/06 (2006.01); B01J 20/28 (2006.01); B01J 35/00 (2006.01); B01J 35/02 (2006.01); B01J 35/04 (2006.01);
U.S. Cl.
CPC ...
B01J 19/2485 (2013.01); B01J 8/067 (2013.01); C10G 2/341 (2013.01); B01J 2219/243 (2013.01); B01J 2219/2428 (2013.01); B01J 2219/2434 (2013.01); B01J 2219/2445 (2013.01); B01J 2219/2446 (2013.01); B01J 2219/32296 (2013.01); B01J 2219/32408 (2013.01); B01J 2219/32466 (2013.01);
Abstract

Reactor for Fischer-Tropsch reaction which is carried out in a three-phase system essentially consisting of a reacting gaseous phase, a reacted liquid phase and a solid catalytic phase, wherein the solid catalytic phase consists of packed or structured bodies of catalytic material encaged within at least one honeycomb monolithic structure with a high thermal conductivity.


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