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:
Mar. 23, 2021

Filed:

Oct. 13, 2014
Applicant:

Casale SA, Lugano, CH;

Inventors:

Ermanno Filippi, Castagnola, CH;

Raffaele Ostuni, Lugano, CH;

Assignee:

Casale SA, Lugano, CH;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01J 19/00 (2006.01); C01B 3/38 (2006.01); C01B 3/02 (2006.01); C01B 13/02 (2006.01); C01C 1/04 (2006.01); C01B 3/26 (2006.01); B01J 7/00 (2006.01); C01B 3/48 (2006.01); C01B 3/50 (2006.01);
U.S. Cl.
CPC ...
C01B 3/025 (2013.01); B01J 7/00 (2013.01); C01B 3/26 (2013.01); C01B 3/382 (2013.01); C01B 3/48 (2013.01); C01B 3/50 (2013.01); C01B 13/0229 (2013.01); C01C 1/0405 (2013.01); B01J 2219/00024 (2013.01); C01B 2203/0205 (2013.01); C01B 2203/0233 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/043 (2013.01); C01B 2203/0445 (2013.01); C01B 2203/0475 (2013.01); C01B 2203/068 (2013.01); C01B 2203/0844 (2013.01); C01B 2203/1235 (2013.01); C01B 2203/141 (2013.01); C01B 2203/142 (2013.01); C01B 2210/0046 (2013.01); Y02P 20/52 (2015.11); Y10T 29/49716 (2015.01);
Abstract

A process for producing ammonia make-up synthesis gas and a procedure for revamping a front-end of an ammonia plant for producing ammonia make-up synthesis gas are disclosed, wherein the make-up synthesis gas is produced by means of steam reforming of a hydrocarbon gaseous feedstock; said front-end includes a primary reformer, a secondary reformer, a shift conversion section, a CO2 removal section and optionally a methanation section; a shell-and-tube gas-heated reformer is installed after said secondary reformer, and a portion of the available feedstock is reformed in the tubes of said gas-heated reformer, and heat is provided to the shell side of said gas-heated reformer by at least a portion of product gas leaving the secondary reformer, possibly mixed with product gas leaving the tubes of said gas-heated reformer.


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