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:
Aug. 06, 2024

Filed:

Apr. 12, 2021
Applicants:

Billy G Clark, Dallas, TX (US);

John C Bourdon, Peculiar, MO (US);

Peter J Photos, El Campo, TX (US);

Franklin Hailey Brown, Ii, San Antonio, TX (US);

David Sisk, San Antonio, TX (US);

Inventors:

Billy G Clark, Dallas, TX (US);

John C Bourdon, Peculiar, MO (US);

Peter J Photos, El Campo, TX (US);

Franklin Hailey Brown, II, San Antonio, TX (US);

David Sisk, San Antonio, TX (US);

Assignee:

Streamline Innovations, Inc., San Antonio, TX (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/14 (2006.01); B01D 53/18 (2006.01); B01D 53/30 (2006.01); C01B 17/05 (2006.01); C10L 3/10 (2006.01); G01N 33/00 (2006.01); G05B 19/05 (2006.01);
U.S. Cl.
CPC ...
B01D 53/1468 (2013.01); B01D 53/18 (2013.01); B01D 53/30 (2013.01); C01B 17/05 (2013.01); C10L 3/103 (2013.01); G01N 33/0044 (2013.01); G05B 19/05 (2013.01); B01D 2257/304 (2013.01);
Abstract

A dynamically adjustable rate sulfur recovery process continuously calculates and adjusts sour gas stream operating pressure and/or flow rate to maximize sweet gas output, thereby improving efficiency. A corresponding desulfurization system may include a fixed-sized pressure vessel, a flow control valve that controls the rate of flow of a sour gas stream into the pressure vessel, a sensor that measures sulfur concentration in the sour gas stream, a reagent tank, an oxidizer tank, and a phase separator that separates sweet gas as a gaseous phase after hydrogen sulfide in the sour gas stream in the pressure vessel is converted to elemental sulfur, sulfur species, or both by contact with reagent from the reagent tank and oxidizer from the oxidizer tank. A PLC (programmable logic controller) continuously calculates updated flow rates based on sulfur concentration measurements from the sensor to achieve maximum sweet gas production.


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