Systems and methods for removing components of a gas mixture
US-9433885-B2 · Sep 6, 2016 · US
US2021060484A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021060484-A1 |
| Application number | US-201916960221-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jan 7, 2019 |
| Priority date | Jan 5, 2018 |
| Publication date | Mar 4, 2021 |
| Grant date | — |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention provides an electrochemical CO2 capture device and methods employing proton-coupled redox active species, e.g., a quinone, phenazine, alloxazine, isoalloxazine, or polyoxometalate, whose protonation and deprotonation can be controlled electrochemically to modify the pH of an aqueous solution or aqueous suspension. This change in pH can be used to sequester and release CO2. The CO2 capture device can be used to sequester gaseous CO2 from a point source, such as flue gas, or from ambient air.
Opening claim text (preview).
What is claimed is: 1 . A device for capturing CO 2 comprising a liquid flow path comprising: a) a first region comprising a first inlet and a first outlet and an aqueous solution or suspension comprising a proton-coupled redox active species, wherein the first region is configured to receive a gas comprising CO 2 via the first inlet, allow the gas to contact the aqueous solution or suspension, and to release the gas depleted of CO 2 via the first outlet; b) a second region fluidically connected to the first region and comprising at least one electrode; c) a third region fluidically connected to the second region and comprising a second outlet, wherein the third region is configured to release CO 2 outgassing from the aqueous solution or suspension via the second outlet; and d) a fourth region fluidically connected to the first and third regions and comprising at least one electrode, wherein oxidation of the proton-coupled redox active species releases one or more protons to decrease the pH of the aqueous solution or suspension and reduction of the proton-coupled redox active species takes up one or more protons to increase the pH of the aqueous solution or suspension. 2 . The device of claim 1 , further comprising an ion-conducting barrier disposed between the second and fourth regions. 3 . The device of claim 1 , wherein the third region further comprises a second inlet fluidically connected to the second outlet, wherein the second inlet is connected to a carrier gas source. 4 . The device of claim 1 , wherein the pH in the third region is less than 8. 5 . The device of claim 1 , wherein the pH in the first region is greater than 8. 6 . The device of claim 1 , wherein the proton-coupled redox active species is present in the aqueous solution or suspension at a concentration of at least 0.5 M. 7 . The device of claim 1 , wherein the oxidized form of the proton-coupled redox active species is a quinone, phenazine, alloxazine, isoalloxazine, or polyoxometalate. 8 . The device of claim 1 , wherein the device comprises an electrochemical cell. 9 . The device of claim 1 , wherein the device compromises a plurality of electrochemical cells. 10 . A method of capturing CO 2 , the method comprising the steps of: a) providing an aqueous solution or suspension comprising a proton-coupled redox active species and having a first pH; b) allowing a gas comprising CO 2 to contact the aqueous solution or suspension under conditions for the CO 2 to dissolve into the aqueous solution or suspension; c) converting the pH of the aqueous solution or suspension to a second pH by oxidizing the proton-coupled redox active species; d) allowing the dissolved CO 2 to outgas from the aqueous solution or suspension; and e) converting the pH of the aqueous solution or suspension to a third pH by reducing the proton-coupled redox active species. 11 . The method of claim 10 , wherein the method is carried out in a device of any one of claims 1 - 9 . 12 . The method of claim 10 , wherein the CO 2 is captured from a point source or ambient air. 13 . The method of claim 10 , wherein the second pH is less than 8. 14 . The method of claim 10 , wherein the third pH is greater than 6. 15 . The method of claim 10 , wherein the second pH is converted to the third pH in a single step. 16 . The method of claim 10 , wherein the second pH is converted to the third pH in two or more steps. 17 . The method of claim 10 , wherein the method operates continuously. 18 . The method of claim 10 , wherein the method operates sequentially. 19 . The method of claim 10 , wherein the oxidized form of the proton-coupled redox active species is a quinone, phenazine, alloxazine, isoalloxazine, or polyoxometalate. 20 . The method of claim 10 , wherein the oxidizing in step (b) and/or reducing in step (d) are carried out electrochemically.
Other organic compounds not covered by B01D2252/00 - B01D2252/20494 · CPC title
Selection of liquid materials for use as absorbents · CPC title
Removing carbon dioxide · CPC title
by absorption · CPC title
Reduction of greenhouse gas [GHG] emissions, e.g. CO2 · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.