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. 04, 2023

Filed:

Apr. 30, 2020
Applicant:

Haldor Topsøe A/s, Kgs. Lyngby, DK;

Inventors:

Morten Thellefsen, Hillerød, DK;

Per Aggerholm Sørensen, Kgs. Lyngby, DK;

Martin Møllerhøj, Birkerød, DK;

Mads Lykke, Brønshøj, DK;

Assignee:

HALDOR TOPSØE A/S, Kgs. Lyngby, DK;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C01B 17/02 (2006.01); C01B 17/04 (2006.01); C01B 17/80 (2006.01); B01D 53/86 (2006.01); B01J 19/00 (2006.01); B01J 19/24 (2006.01); C01B 17/775 (2006.01); B01D 53/14 (2006.01); C01B 17/76 (2006.01); F23G 7/06 (2006.01);
U.S. Cl.
CPC ...
C01B 17/0404 (2013.01); B01D 53/1481 (2013.01); B01D 53/1493 (2013.01); B01D 53/8615 (2013.01); B01J 19/0013 (2013.01); B01J 19/2405 (2013.01); B01J 19/2465 (2013.01); C01B 17/0253 (2013.01); C01B 17/0447 (2013.01); C01B 17/0452 (2013.01); C01B 17/0456 (2013.01); C01B 17/76 (2013.01); C01B 17/775 (2013.01); C01B 17/80 (2013.01); C01B 17/806 (2013.01); F23G 7/06 (2013.01); B01D 2255/20723 (2013.01); B01J 2219/00157 (2013.01); C01P 2006/80 (2013.01); F23G 2209/14 (2013.01);
Abstract

A process plant and a process for production of sulfur from a feedstock gas including from 15% to 100 vol % HS and a stream of sulfuric acid, the process including a) providing a Claus reaction furnace feed stream with a substoichiometric amount of oxygen, b) directing to a Claus reaction furnace operating at elevated temperature, c) cooling to provide a cooled Claus converter feed gas, d) directing to contact a material catalytically active in the Claus reaction, e) withdrawing a Claus tail gas and elementary sulfur, f) directing a stream comprising said Claus tail gas to a Claus tail gas treatment, wherein sulfuric acid directed to said Claus reaction furnace is in the form of droplets with 90% of the mass of the droplets having a diameter below 500 μm, with the associated benefit of such a process efficiently converting all liquid HSOto gaseous HSOand further to SO.


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