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:
May. 11, 2021

Filed:

Aug. 13, 2018
Applicants:

David W. Maher, Spring, TX (US);

Shwetha Ramkumar, Cypress, TX (US);

P. Scott Northrop, The Woodlands, TX (US);

Robert D. Denton, Bellaire, TX (US);

Inventors:

David W. Maher, Spring, TX (US);

Shwetha Ramkumar, Cypress, TX (US);

P. Scott Northrop, The Woodlands, TX (US);

Robert D. Denton, Bellaire, TX (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/14 (2006.01); B01D 61/24 (2006.01); C10L 3/10 (2006.01); B01D 53/18 (2006.01); B01D 53/22 (2006.01); B01D 11/00 (2006.01);
U.S. Cl.
CPC ...
B01D 53/1462 (2013.01); B01D 53/1418 (2013.01); B01D 53/1425 (2013.01); B01D 53/185 (2013.01); B01D 53/229 (2013.01); B01D 61/246 (2013.01); C10L 3/103 (2013.01); C10L 3/104 (2013.01); C10L 3/106 (2013.01); B01D 2011/007 (2013.01); B01D 2252/204 (2013.01); B01D 2256/245 (2013.01); B01D 2257/304 (2013.01); B01D 2257/504 (2013.01); C10L 2290/06 (2013.01); C10L 2290/10 (2013.01); C10L 2290/46 (2013.01); C10L 2290/541 (2013.01); C10L 2290/545 (2013.01); C10L 2290/548 (2013.01);
Abstract

A method of separating impurities from a natural gas stream. The natural gas stream is cooled through heat exchange with one or more process streams to produce a chilled gas stream, which is contacted with a lean solvent stream in a contactor to separate hydrogen sulfide (HS) from the chilled gas stream, thereby producing a rich solvent stream and a partially-treated gas stream. Carbon dioxide (CO) and HS are separated from the partially-treated gas stream in a membrane separation system, thereby creating a fully-treated gas stream and a permeate gas stream, the permeate gas stream being comprised primarily of HS and CO, and the fully-treated gas stream being comprised primarily of natural gas. The fully-treated gas stream and the permeate gas stream are at a lower temperature than the partially-treated gas stream. The fully-treated gas stream and the permeate gas stream comprise the one or more process streams.


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