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:
Oct. 02, 2018

Filed:

May. 12, 2011
Applicants:

Ermanno Filippi, Castagnola, CH;

Francesco Baratto, Como, IT;

Sergio Panza, Como, IT;

Raffaele Ostuni, Milan, IT;

Inventors:

Ermanno Filippi, Castagnola, CH;

Francesco Baratto, Como, IT;

Sergio Panza, Como, IT;

Raffaele Ostuni, Milan, IT;

Assignee:

Casale SA, Lugano, CH;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 3/02 (2006.01); C01B 3/38 (2006.01); C01B 3/48 (2006.01); C01B 3/50 (2006.01); C01B 3/56 (2006.01);
U.S. Cl.
CPC ...
C01B 3/025 (2013.01); C01B 3/382 (2013.01); C01B 3/48 (2013.01); C01B 3/506 (2013.01); C01B 3/56 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/0288 (2013.01); C01B 2203/043 (2013.01); C01B 2203/046 (2013.01); C01B 2203/0445 (2013.01); C01B 2203/0475 (2013.01); C01B 2203/068 (2013.01); C01B 2203/0883 (2013.01); C01B 2203/1235 (2013.01); C01B 2203/141 (2013.01); C01B 2203/143 (2013.01); C01B 2203/146 (2013.01);
Abstract

A process for producing ammonia synthesis gas from a hydrocarbon-containing feedstock, with steps of primary reforming, secondary reforming with an oxidant stream, and further treatment of the synthesis gas including shift, removal of carbon dioxide and methanation, wherein the synthesis gas delivered by secondary reforming is subject to a medium-temperature shift (MTS) at a temperature between 200 and 350° C., and primary reforming is operated with a steam-to-carbon ratio lower than 2. A corresponding method for revamping an ammonia plant is disclosed, where an existing HTS reactor is modified to operate at medium temperature, or replaced with a new MTS reactor, and the steam-to-carbon ratio in the primary reformer is lowered to a value in the range 1-5−2, thus reducing inert steam in the flow rate trough the equipments of the front-end.


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