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:
Jun. 11, 2024

Filed:

Nov. 15, 2023
Applicant:

Airmyne, Inc., Berkeley, CA (US);

Inventors:

Bart Ludo Scherpbier, San Francisco, CA (US);

Jun Seon Hong, Berkeley, CA (US);

Derek Chase Popple, Sacramento, CA (US);

Mark Patrick Cyffka, El Cerrito, CA (US);

Aryaman Bhartia, Berkeley, CA (US);

Cyndia Aiyun Cao, Oakland, CA (US);

Arun Suresh Kamath, Berkeley, CA (US);

Sudip Mukhopadhyay, Berkeley, CA (US);

Assignee:

AirMyne, Inc., Berkeley, CA (US);

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
B01D 53/14 (2006.01); B01D 53/18 (2006.01); B01D 53/62 (2006.01); B01D 53/78 (2006.01);
U.S. Cl.
CPC ...
B01D 53/1493 (2013.01); B01D 53/1406 (2013.01); B01D 53/1412 (2013.01); B01D 53/1425 (2013.01); B01D 53/1475 (2013.01); B01D 53/185 (2013.01); B01D 53/62 (2013.01); B01D 53/78 (2013.01); B01D 2251/60 (2013.01); B01D 2251/80 (2013.01); B01D 2252/204 (2013.01); B01D 2252/20494 (2013.01); B01D 2252/504 (2013.01); B01D 2252/602 (2013.01); B01D 2257/504 (2013.01); B01D 2258/0283 (2013.01);
Abstract

In a general aspect, a carbon dioxide removal system is presented. In some cases, a gas-liquid contactor is wetted with an alkaline capture solution. A first flow from a first gaseous feed including COfrom a first source is directed to interact with the alkaline capture solution in the gas-liquid contactor, which forms a first CO-rich alkaline capture solution. A second flow from a second gaseous feed including COfrom a second, distinct source is directed to interact with the first CO-rich alkaline capture solution, which forms a second CO-rich alkaline capture solution. In some cases, the second flow is independent of the first gaseous feed, and a concentration of COin the second CO-rich alkaline capture solution is higher than a concentration of COin the first CO-rich alkaline capture solution. COcan be separated from the second CO-rich alkaline capture solution.


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