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:
Apr. 04, 2017

Filed:

Sep. 10, 2015
Applicant:

Chevron U.s.a. Inc., San Ramon, CA (US);

Inventor:

Joshua Allen Thompson, Martinez, CA (US);

Assignee:

Chevron U.S.A. Inc., San Ramon, CA (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/047 (2006.01); B01J 20/18 (2006.01);
U.S. Cl.
CPC ...
B01D 53/0476 (2013.01); B01J 20/18 (2013.01); B01D 2253/108 (2013.01); B01D 2256/24 (2013.01); B01D 2256/245 (2013.01); B01D 2257/304 (2013.01); B01D 2257/504 (2013.01); B01D 2259/4003 (2013.01); B01D 2259/404 (2013.01); B01D 2259/40018 (2013.01); B01D 2259/40041 (2013.01); B01D 2259/40049 (2013.01); B01D 2259/41 (2013.01);
Abstract

Disclosed are methods for removing acid gas from a feed stream of natural gas including acid gas, methane and ethane. The methods include alternating input of the feed stream between at least two beds of adsorbent particles comprising zeolite SSZ-13 such that the feed stream contacts one of the at least two beds at a given time in an adsorption step and a tail gas stream is simultaneously vented from another of the at least two beds in a desorption step. The contact occurs at a feed pressure of from about 50 to about 1000 psia for a sufficient period of time to preferentially adsorb acid gas from the feed stream. A product gas stream is produced containing no greater than about 2 mol % carbon dioxide and at least about 65 mol % of methane recovered from the feed stream and at least about 25 mol % of ethane recovered from the feed stream. The feed stream is input at a feed end of each bed. The product gas stream is removed from a product end of each bed. The tail gas stream is vented from the feed end of each bed. The methods require lower vacuum power consumption and allow improved hydrocarbon recoveries compared with known methods.


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