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:
Feb. 25, 2020

Filed:

Jan. 24, 2018
Applicant:

Air Liquide Advanced Technologies U.s. Llc, Houston, TX (US);

Inventor:

Michael J. Mitariten, Pittstown, NJ (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D 53/22 (2006.01); B01D 53/26 (2006.01); B01D 53/04 (2006.01); B01D 53/047 (2006.01); B01D 71/56 (2006.01); B01D 71/52 (2006.01); B01D 71/76 (2006.01); C07C 7/00 (2006.01); C07C 7/12 (2006.01); C07C 7/144 (2006.01);
U.S. Cl.
CPC ...
B01D 53/226 (2013.01); B01D 53/047 (2013.01); B01D 53/0446 (2013.01); B01D 53/0462 (2013.01); B01D 53/229 (2013.01); B01D 53/265 (2013.01); B01D 71/52 (2013.01); B01D 71/56 (2013.01); B01D 71/76 (2013.01); C07C 7/005 (2013.01); C07C 7/12 (2013.01); C07C 7/144 (2013.01); B01D 2256/245 (2013.01); B01D 2257/304 (2013.01); B01D 2257/504 (2013.01); B01D 2257/556 (2013.01); B01D 2257/702 (2013.01); B01D 2257/708 (2013.01); B01D 2257/80 (2013.01);
Abstract

The invention relates to a process for recovering methane from digester biogas or landfill gas. More specifically, the invention pertains to biomethane production that substantially removes carbon dioxide from a digester biogas or landfill gas using first, second, and third purification stages each comprising one or more membranes selective for carbon dioxide over methane. A retentate from the first stage is separated by the one more membranes of the second stage into a second state retentate, forming a biomethane product gas. A permeate from the first stage is separated by the one or more membranes of the third stage into a third stage retentate and a third stage permeate. Recovery of methane from the biogas is boosted by feeding the third stage retentate to the first purification stage. The recovery may be optionally further boosted by compressing the second stage permeate with the biogas at a main compressor.


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