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:
Jan. 12, 2021

Filed:

Sep. 05, 2019
Applicant:

Honeywell International Inc., Morristown, NJ (US);

Inventors:

Jan De Ren, Bracknell, GB;

William J. Whyman, Tulsa, OK (US);

David A. Roman, Guildford, GB;

Tom M. Jackson, Surrey, GB;

Assignee:

HONEYWELL INTERNATIONAL INC., Morristown, NJ (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/76 (2006.01); B01D 53/78 (2006.01); B01D 53/50 (2006.01); B01D 53/56 (2006.01); B01D 53/72 (2006.01); C10G 27/04 (2006.01);
U.S. Cl.
CPC ...
B01D 53/76 (2013.01); B01D 53/50 (2013.01); B01D 53/56 (2013.01); B01D 53/72 (2013.01); B01D 53/78 (2013.01); C10G 27/04 (2013.01); C10G 2300/1003 (2013.01); C10G 2300/202 (2013.01); C10G 2300/207 (2013.01); C10G 2300/4056 (2013.01); C10G 2300/4081 (2013.01);
Abstract

An integrated mercaptan extraction and/or sweetening and thermal oxidation and flue gas treatment process for a wide variety of sulfur, naphthenic, phenolic/cresylic contaminated waste streams is described. It provides comprehensive treatment for the safe disposal of sulfidic, naphthenic, phenolic/cresylic spent caustic streams, disulfide streams, spent air streams, spent mixed amine and caustic streams (also known as COS solvent streams) from sulfur treating processes. It allows the use of regenerated spent caustic in the sulfur oxide removal section of the thermal oxidation system reducing the need for fresh NaOH. It may also contain an integrated make-up water system. The integration allows the use of the liquefied petroleum gas or other hydrocarbon feeds to the respective extraction or sweetening process to offset external fuel gas requirements for the thermal oxidation system and for the push/pull system of the spent caustic surge drum and optional hydrocarbon surge drum.


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