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. 17, 2018

Filed:

Aug. 05, 2014
Applicant:

Dow Global Technologies Llc, Midland, MI (US);

Inventors:

Scott T. Matteucci, Midland, MI (US);

H. Robert Goltz, Midland, MI (US);

Ajay N. Badhwar, Houston, TX (US);

Nicholas J. Shurgott, Rosharon, TX (US);

Assignee:

Dow Global Technologies LLC, Midland, MI (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10L 3/10 (2006.01); B01J 20/26 (2006.01); B01D 53/04 (2006.01); B01D 53/047 (2006.01); B01J 20/30 (2006.01); B01J 20/20 (2006.01); B01J 20/28 (2006.01); B01J 20/34 (2006.01);
U.S. Cl.
CPC ...
C10L 3/101 (2013.01); B01D 53/047 (2013.01); B01D 53/0462 (2013.01); B01J 20/20 (2013.01); B01J 20/267 (2013.01); B01J 20/28057 (2013.01); B01J 20/28066 (2013.01); B01J 20/28085 (2013.01); B01J 20/28092 (2013.01); B01J 20/3078 (2013.01); B01J 20/3416 (2013.01); B01J 20/3425 (2013.01); B01J 20/3441 (2013.01); B01D 2253/202 (2013.01); B01D 2253/306 (2013.01); B01D 2253/308 (2013.01); B01D 2256/245 (2013.01); B01D 2257/7022 (2013.01); C10L 2290/542 (2013.01);
Abstract

A method is disclosed for the separation of ethane and heavier hydrocarbons or propane and heavier hydrocarbons from natural gas to provide a methane-rich natural gas stream and less volatile natural gas liquids (NGLs). This method provides for the use of a regenerable adsorbent media comprising a porous cross-linked polymeric adsorbent, a pyrolized macroporous polymer, or mixtures thereof, which is regenerated by a pressure swing adsorption (PSA) process, temperature swing adsorption (TSA) process, or combination of the two. Said regeneration step may be operated as a batch process, a semi-continuous process, or preferably as a continuous process.


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