Systems and Methods for Producing Carbon Solids
US-2024417566-A1 · Dec 19, 2024 · US
US2016281245A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2016281245-A1 |
| Application number | US-201415038126-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 20, 2014 |
| Priority date | Nov 20, 2013 |
| Publication date | Sep 29, 2016 |
| Grant date | — |
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Disclosed herein are various layered, carbon-containing materials for use in reducing carbon dioxide. In certain embodiments, the materials comprise single wall carbon nanotubes (SWNTs).
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Therefore, at least the following is claimed: 1 . A method, comprising: providing an electrolyte including dissolved carbon dioxide (CO 2 ) to an sp 2 bonded carbon electrode; and reducing the dissolved CO 2 via electroreduction by powering the sp 2 bonded carbon electrode. 2 . The method of claim 1 , further comprising mixing CO 2 with the electrolyte to produce the electrolyte including dissolved CO 2 . 3 . The method of claim 1 , wherein the CO 2 is remotely mixed with the electrolyte. 4 . The method of claim 1 , wherein the CO 2 diffuses through a lyophobic, porous membrane to mix with the electrolyte. 5 . The method of claim 1 , wherein the sp 2 bonded carbon electrode comprises carbon nanotubes, carbon nanofibers, a carbon-carbon compact, a multilayer graphene film, reduced graphene oxide, pyrolytic graphite, and/or microcrystalline graphite. 6 . The method of claim 1 , wherein the sp 2 bonded carbon electrode comprises single wall carbon nanotubes. 7 . The method of claim 1 , wherein the atomic percent of carbon in the sp 2 bonded carbon electrode is at least about 70%. 8 . The method of claim 1 , wherein the sp 2 bonded carbon electrode has a layered structure. 9 . The method of claim 8 , wherein the space between at least two adjacent layers of the layered structure is at least about 0.1 nm. 10 . The method of claim 1 , wherein the sp 2 bonded carbon electrode has a sheet resistance of about 500 ohms/sq or less. 11 . The method of claim 1 , wherein CO 2 reduction initiates at an overpotential of about 1 V or less. 12 . The method of claim 1 , wherein CO 2 reduction produces at least one of formate, acetate, carbon monoxide, methanol, ethanol, methane, ethane, formaldehyde, or acetaldehyde. 13 . A carbon dioxide (CO 2 ) reduction cell, comprising: a layered, sp 2 bonded carbon material; a lyophobic, porous membrane comprising a first side and a second side opposite the first side, the layered, sp 2 bonded carbon material disposed on the first side of the membrane; a chamber on the second side of the membrane, the chamber including CO 2 ; and an electrolyte volume on the first side of the membrane, the electrolyte volume including an electrolyte in contact with the layered, sp 2 bonded carbon material, where CO 2 diffuses from the chamber through the membrane into the electrolyte and supplying power to the layered, sp 2 bonded carbon material reduces the CO 2 in the electrolyte. 14 . The CO 2 reduction cell of claim 13 , wherein the CO 2 reduction produces at least one of formic acid ions, carbon monoxide, methanol, ethanol, methane or ethane, acetic acid, formaldehyde, acetaldehyde. 15 . The CO 2 reduction cell of claim 13 , wherein the electrolyte wets the layered, sp 2 bonded carbon material through to the first side of the membrane. 16 . The CO 2 reduction cell of claim 13 , wherein the electrolyte comprises dimethylformamide (DMF), tetrabutylammonium hexafluorophosphate (TBAPF 6 ), tetrabutylammonium tetrafluoroborate (TBABF 4 ), and water (H 2 O). 17 . The CO 2 reduction cell of claim 13 , wherein the layered, sp 2 bonded carbon material comprises a single wall carbon nanotube (SWNT) film. 18 . The CO 2 reduction cell of claim 17 , wherein the SWNT film is about 1.5 μm thick. 19 . The CO 2 reduction cell of claim 17 , wherein the SWNT film has been electrochemically activated. 20 . The CO 2 reduction cell of claim 13 , wherein the membrane is a PTFE membrane. 21 . The CO 2 reduction cell of claim 13 , further comprising a power supply coupled to the layered, sp 2 bonded carbon material. 22 . The CO 2 reduction cell of claim 13 , wherein the power supply is coupled to the layered, sp 2 bonded carbon material via a contact electrode that overlaps a portion of the layered, sp 2 bonded carbon material. 23 . A method, comprising: providing a gas phase medium including CO 2 to a first side of a lyophobic, porous membrane, where at least a portion of the CO 2 diffuses through the lyophobic, porous membrane into an electrolyte in contact with a second side of the lyophobic, porous membrane; and providing power to a sp 2 bonded carbon material film disposed on the second side of the lyophobic, porous membrane, where powering the sp 2 bonded carbon material reduces the CO 2 in the electrolyte. 24 . The method of claim 23 , wherein the sp 2 bonded carbon material comprises a single wall carbon nanotube (SWNT) film. 25 . The method of claim 24 , wherein CO 2 reduction initiates at an overpotential of about 0.05 V. 26 . The method of claim 24 , wherein a power supply provides power to the SWNT film via a contact electrode that overlaps a portion of the SWNT film. 27 . The method of claim 26 , wherein the power supply is coupled between the SWNT film and an anode in contact with the electrolyte. 28 . The method of claim 23 , wherein the CO 2 reduction produces at least one of formic acid ions, acetic acid ions, carbon monoxide, methanol, ethanol, methane, ethane, formaldehyde, or acetaldehyde.
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