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. 21, 2021

Filed:

Mar. 07, 2018
Applicant:

Haldor Topsøe A/s, Kgs. Lyngby, DK;

Inventors:

Christian Henrik Speth, Lynge, DK;

Per Juul Dahl, Vedbæk, DK;

Annette E. Krøll Jensen, Fredensborg, DK;

Niels Christian Schjødt, Hvalsø, DK;

Marcus Symreng, Malmö, SE;

Assignee:

Haldor Topsoe A/S, Lyngby, DK;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01C 1/04 (2006.01); C01B 3/02 (2006.01); B01D 19/00 (2006.01); B01J 23/80 (2006.01); C01B 3/48 (2006.01); C01B 3/52 (2006.01); C07C 273/10 (2006.01);
U.S. Cl.
CPC ...
C01C 1/0405 (2013.01); B01D 19/001 (2013.01); B01J 23/80 (2013.01); C01B 3/025 (2013.01); C01B 3/48 (2013.01); C01B 3/52 (2013.01); C01C 1/0488 (2013.01); C07C 273/10 (2013.01); C01B 2203/0244 (2013.01); C01B 2203/0283 (2013.01); C01B 2203/048 (2013.01); C01B 2203/0415 (2013.01); C01B 2203/068 (2013.01); C01B 2203/1076 (2013.01); C01B 2203/1241 (2013.01); C01B 2203/1258 (2013.01); C01B 2203/169 (2013.01);
Abstract

A process for producing an ammonia synthesis gas, said process comprising the steps of: —Reforming a hydrocarbon feed in a reforming step thereby obtaining a synthesis gas comprising CH, CO, CO, Hand HO, —Shifting the synthesis gas in one in or more shift steps in series, —Optionally wash the synthesis gas leaving the shift section with water, —Sending the process condensate originating from cooling and washing the synthesis gas leaving the shift section to a process condensate stripper wherein the dissolved shift byproducts and dissolved gases are stripped out of the process condensate using steam resulting in a steam stream containing more than 99% of the dissolved methanol in process condensate. —Adding all or part of said steam stream from the process condensate stripper to the synthesis gas downstream the reforming step, prior to the last shift step, wherein —The steam/carbon ratio in the reforming step and the shift step is less than 2.6.


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