ELECTROCHEMICAL CO2 CAPTURE WITH AIR STABLE REDOX SPECIES
20250144562 ยท 2025-05-08
Inventors
- Yan JING (Cambridge, MA, US)
- Shijian Jin (Cambridge, MA, US)
- Roy G. Gordon (Cambridge, MA)
- Michael J. Aziz (Cambridge, MA, US)
Cpc classification
International classification
B01D53/32
PERFORMING OPERATIONS; TRANSPORTING
B01D53/96
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The invention features solutions of water-soluble, oxygen-resistant redox-active species circulated in flow cells to electrochemically capture CO.sub.2 from air or flue gas and release pure CO.sub.2. The method is safe, scalable, and potentially inexpensive, as it utilizes non-volatile and potentially low-cost redox organic and inexpensive inorganic species and can operate at ambient temperature and pressure and can operate at high current densities.
Claims
1. A method for capturing CO.sub.2 comprising: a) providing an electrochemical cell comprising a redox-active species dissolved or dispersed in aqueous solution; b) electrochemically reducing the redox-active species to a reduced state; and c) contacting a mixture of gases comprising CO.sub.2 with the aqueous solution; wherein the redox-active species comprises an aromatic redox core and one or more substituents which increase resistance of the reduced state to oxidation by oxygen or wherein a redox potential of the redox-active species and its reduced state is stable to oxidation by oxygen.
2. The method of claim 1, wherein the one or more substituents comprises one or more electron withdrawing groups.
3. The method of claim 2, wherein the electron withdrawing groups are separated from the redox core by (CH.sub.2).sub.1-6, O(CH.sub.2).sub.0-6, S(CH.sub.2).sub.0-6, NH(CH.sub.2).sub.0-6, or NR.sub.a(CH.sub.2).sub.0-6.
4. The method of claim 1, wherein the one or more substituents comprise one or more groups selected from NO.sub.2, CN, SO.sub.3R.sub.a, CHO, C(O)R.sub.a, C(O)O C(O)R.sub.a, C(O)OR.sub.a, CONH.sub.2, COO.sup., NR.sub.a3.sup.+, CF.sub.3, SO.sub.2R.sub.a, F, Cl, Br, I, OR.sub.a, SR.sub.a, P(O)(OR.sub.a).sub.2,(CH.sub.2).sub.1-3NO.sub.2, (CH.sub.2).sub.1-3CN, (CH.sub.2).sub.1-3SO.sub.3R.sub.a, (CH.sub.2).sub.1-3CHO, (CH.sub.2).sub.1-3C(O)R.sub.a, (CH.sub.2).sub.1-3C(O)OCOR.sub.a, (CH.sub.2).sub.1-3COOR.sub.a, (CH.sub.2).sub.1-3C(O)OH, (CH.sub.2).sub.1-3CONH.sub.2, (CH.sub.2).sub.1-3C(O)O, (CH.sub.2).sub.1-3NR.sub.a3,(CH.sub.2).sub.1-3SO.sub.2R.sub.a, CH.sub.2CF.sub.3, CH.sub.2CCl.sub.3, CH.sub.2CBr.sub.3, CH.sub.2Cl.sub.3, CH.sub.2CHF.sub.2, CH.sub.2CHCl.sub.2, CH.sub.2CHBr.sub.2, CH.sub.2CHI.sub.2, CH.sub.2(CF.sub.2).sub.1-6CF.sub.3,(CH.sub.2).sub.1-3OR.sub.a, and (CH.sub.2).sub.1-3SR.sub.a, wherein each R.sub.a is independently H; optionally substituted C.sub.1-6 alkyl; optionally substituted C.sub.3-10 carbocyclyl; or optionally substituted C.sub.1-9 heterocyclyl having one to four heteroatoms independently selected from O, N, and S.
5. The method of claim 1, wherein the one or more substituents are optionally substituted C.sub.1-6 alkyl groups comprising a quaternary ammonium group, optionally substituted C.sub.1-6 alkoxy groups comprising a quaternary ammonium group, or optionally substituted C.sub.1-6 alkyl thio groups comprising a quaternary ammonium group.
6. The method of claim 1, wherein the one or more substituents comprise at least one (CH.sub.2).sub.1-11NR.sub.a3.sup.+ group, wherein each R.sub.a is independently H; optionally substituted C.sub.1-6 alkyl; optionally substituted C.sub.3-10 carbocyclyl; optionally substituted C.sub.1-9 heterocyclyl having one to four heteroatoms independently selected from O, N, and S; optionally substituted C.sub.6-20 aryl; optionally substituted C.sub.1-9 heteroaryl having one to four heteroatoms independently selected from O, N, and S; an oxygen protecting group; or a nitrogen protecting group.
7. The method of any one of claims 1-6, wherein the aromatic redox core is para or ortho benzoquinone, naphthoquinone, anthraquinone, phenanthrenequinone, fluorenone, benzophenone, anthrone, xanthone, thioxanthone, acridone, phenazine, viologen, alloxazine, isoalloxazine, azobenzene, phthalimide, phenothiazine, naphthalimide, pyromellitic diimide, 1,4,5,8-naphthalenetetracarbodiimide, or benzo(c)cinnoline.
8. The method of claim 7, wherein the redox-active species has the formula: ##STR00011## ##STR00012## ##STR00013## wherein dashed bonds are single or double bonds; wherein X is N or NR.sup.X, Y.sub.1 is O or S, Y.sub.2 is C(R.sup.6).sub.2, NR.sup.Y, S, O, and Z is CR.sup.6, CO, CS, CNR.sup.Z, or CNH.sup.+R.sup.Z; wherein each R.sup.N1, R.sup.N2, R.sup.X, R.sup.Y, and R.sup.Z is independently selected from CH.sub.2R.sup.EWG; CH.sub.2R.sup.QA; H; optionally substituted C.sub.1-6 alkyl; optionally substituted C.sub.3-10 carbocyclyl; optionally substituted C.sub.1-9 heterocyclyl having one to four heteroatoms independently selected from O, N, and S; optionally substituted C.sub.6-20 aryl; optionally substituted C.sub.1-9 heteroaryl having one to four heteroatoms independently selected from O, N, and S; and a nitrogen protecting group; wherein each of R.sup.1, R.sup.2, R.sup.3, R.sup.4, R.sup.5, R.sup.6, R.sup.7, R.sup.8, R.sup.9, and R.sup.10 is independently selected from R.sup.EWG; R.sup.QA; H; halo; optionally substituted C.sub.1-6 alkyl; oxo; optionally substituted C.sub.3-10 carbocyclyl; optionally substituted C.sub.1-9 heterocyclyl having one to four heteroatoms independently selected from O, N, and S; optionally substituted C.sub.6-20 aryl; optionally substituted C.sub.1-9 heteroaryl having one to four heteroatoms independently selected from O, N, and S; and P(O)R.sub.a2; P(O)(OR.sub.a).sub.2; or any two adjacent groups selected from R.sup.1, R.sup.2, R.sup.3, and R.sup.4 are joined to form an optionally substituted 3-6 membered ring, or an ion thereof, wherein each R.sub.a is independently H; optionally substituted C.sub.1-6 alkyl; optionally substituted C.sub.3-10 carbocyclyl; optionally substituted C.sub.1-9 heterocyclyl having one to four heteroatoms independently selected from O, N, and S; optionally substituted C.sub.6-20 aryl; optionally substituted C.sub.1-9 heteroaryl having one to four heteroatoms independently selected from O, N, and S; an oxygen protecting group; and a nitrogen protecting group; wherein each R.sup.EWG is independently selected from NO.sub.2, CN, SO.sub.3R.sub.a, CHO, C(O)R.sub.a, C(O)O C(O)R.sub.a, C(O)OR.sub.a, CONH.sub.2, COO.sup., NR.sub.a3.sup.+, CF.sub.3, SO.sub.2R.sub.a, F, Cl, Br, I, OR.sub.a, SR.sub.a, P(O)(OR.sub.a).sub.2,(CH.sub.2).sub.1-3NO.sub.2, (CH.sub.2).sub.1-3CN, (CH.sub.2).sub.1-3SO.sub.3R.sub.a, (CH.sub.2).sub.1-3CHO, (CH.sub.2).sub.1-3C(O)R.sub.a, (CH.sub.2).sub.1-3C(O)OCOR.sub.a, (CH.sub.2).sub.1-3COOR.sub.a, (CH.sub.2).sub.1-3C(O)OH, (CH.sub.2).sub.1-3CONH.sub.2, (CH.sub.2).sub.1-3C(O)O, (CH.sub.2).sub.1- .sub.3NR.sub.a3.sup.+,(CH.sub.2).sub.1-3SO.sub.2R.sub.a, CH.sub.2CF.sub.3, CH.sub.2CCl.sub.3, CH.sub.2CBr.sub.3, CH.sub.2Cl.sub.3, CH.sub.2CHF.sub.2, CH.sub.2CHCl.sub.2, CH.sub.2CHBr.sub.2, CH.sub.2CHI.sub.2, CH.sub.2(CF.sub.2).sub.1-6CF.sub.3,(CH.sub.2).sub.1-3OR.sub.a, and (CH.sub.2).sub.1-3SR.sub.a, wherein each R.sub.a is independently H; optionally substituted C.sub.1-6 alkyl; optionally substituted C.sub.3-10 carbocyclyl; or optionally substituted C.sub.1-9 heterocyclyl having one to four heteroatoms independently selected from O, N, and S; wherein each R.sup.QA is independently selected from (CH.sub.2).sub.1-6NR.sub.a3.sup.+, O(CH.sub.2).sub.1-6NR.sub.a3.sup.+, S(CH.sub.2).sub.1-6NR.sub.a3.sup.+, NR.sub.a(CH.sub.2).sub.1-6NR.sub.a3.sup.+, and N((CH.sub.2).sub.1-6NR.sub.a3.sup.+).sub.2, wherein each R.sub.a is independently H; optionally substituted C.sub.1-6 alkyl; optionally substituted C.sub.3-10 carbocyclyl; or optionally substituted C.sub.1-9 heterocyclyl having one to four heteroatoms independently selected from O, N, and S; wherein at least one of R.sup.1, R.sup.2, R.sup.3, R.sup.4, R.sup.5, R.sup.6, R.sup.7 and R.sup.8 is R.sup.EWG or R.sup.QA and/or at least one R.sup.N1, R.sup.N2, R.sup.X, R.sup.Y, or R.sup.Z, is CH.sub.2R.sup.EWG or CH.sub.2R.sup.QA.
9. The method of claim 1, wherein the redox-active species is: ##STR00014## ##STR00015## ##STR00016## ##STR00017##
10. The method of any one of claims 1-9, wherein step b) produces hydroxide ions and step c) comprises forming inorganic carbonates.
11. The method of any one of claims 1-9, wherein the reduced state reacts with one or more CO.sub.2 molecules to form a CO.sub.2 adduct.
12. The method of any one of claims 1-11, wherein in step (b) the reduced state reacts with water to produce one or more hydroxide ions.
13. The method of any one of claims 1-12, further comprising electrochemically oxidizing the reduced state to release CO.sub.2.
14. The method of claim 1, wherein the redox-active species is an inorganic redox-active species.
15. The method of claim 14, wherein the redox-active species comprises a nitrate anion and the reduced state comprises a nitrite anion.
16. The method of claim 14 or 15, wherein the aqueous solution comprises a catalyst or enzyme to reduce an overpotential of reduction of the redox-active species and/or oxidation of the reduced state.
17. The method of claim 16, wherein the catalyst comprises Pt, Ir, Pd, Ni, Rh, Ru, Zn, Cu, Fe, or Co, or a combination thereof; or wherein the catalyst comprises an aminoxyl radical or phthalimido-N-oxyl radical; or wherein the enzyme is an alcohol dehydrogenase.
18. The method of any one of claims 15-17, further comprising oxidizing the nitrite anion to a nitrate anion and releasing the captured CO.sub.2.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0054]
[0055]
[0056]
[0057]
[0058]
[0059]
[0060]
[0061]
[0062]
[0063]
[0064]
[0065]
DETAILED DESCRIPTION OF THE INVENTION
[0066] The invention provides electrochemically cycled methods of capturing CO.sub.2, e.g., from air or flue gas, and releasing pure CO.sub.2, using water-soluble oxygen-resistant redox-active species circulated in flow cells.
[0067] The method is safe, scalable, and potentially inexpensive, as it utilizes non-volatile and potentially low-cost redox organic and inexpensive inorganic species, can operate at ambient temperature and pressure, and can operate at high current densities.
[0068] The capture method involves either a pH-swing cycle or a nucleophilicity-swing cycle of dissolved redox-active species, electrochemically driven through the proton-coupled electron transfer (PCET) or CO.sub.2-coupled electron transfer. In pH-swing cycle capture, redox organics (RO, e.g., an anthraquinone) or redox inorganics (RI, e.g., a nitrate salt) react with water, e.g., to become, e.g., ROH.sub.2 (e.g., an anthrahydroquinone), or, e.g., RI.sup.n (e.g., a nitrite salt), during the electrochemical reduction and produce hydroxides which react with CO.sub.2 and form inorganic (bi)carbonates (e.g., HCO.sub.3.sup., CO.sub.3.sup.2). In nucleophilicity-swing capture, ROs become nucleophiles after reduction which can react with CO.sub.2 directly to form organic carbonates (e.g., RO(CO.sub.2).sub.2.sup.2, e.g., where RO is a quinone, e.g., an anthraquinone, core).
[0069] During the electrochemical oxidation, ROs can release protons that react with inorganic (bi)carbonates and release CO.sub.2; or ROs lose affinity for CO.sub.2 and release pure CO.sub.2. During the electrochemical oxidation, reduced RIs such as the nitrate/nitrite redox couple can consume hydroxide ions thereby lowering the pH and allowing release of CO.sub.2.
[0070] In both mechanisms of capture involving ROs, a reduced state of ROs is required for CO.sub.2 capture. However, reduced ROs are oxygen sensitive, and atmospheric O.sub.2 can chemically oxidize reduced ROs back to the oxidized state of ROs, which do not have CO.sub.2 affinity (
Redox Organics
[0071] In this invention, we enhance air-stability of reduced ROs through inclusion of one or multiple functional groups on the redox cores. The functional group may be attached to the redox core at any possible position, e.g., any position that would otherwise be occupied by H. The introduced functional groups could be the same, or different. Redox cores include, but are not limited to, para or ortho benzoquinone, naphthoquinone, anthraquinone, phenanthrenequinone, fluorenone, benzophenone, anthrone, xanthone, thioxanthone, acridone, phenazine, viologen, alloxazine, isoalloxazine, azobenzene, phthalimide, phenothiazine, naphthalimide, pyromellitic diimide, 1,4,5,8-naphthalenetetracarbodiimide, or benzo(c)cinnoline. Specific formulas are provided in formulas (I)(XX). Redox organics may be present in a mixture.
[0072] Organic redox-active species may include multiple electron-withdrawing groups to elevate redox potentials to be comparable to or higher than the 02 reduction potential at the pH of interest, so that the oxidation of the reduced molecules by 02 is thermodynamically less favored, or even disfavored. The electron-withdrawing groups can be directly connected to the redox cores, or indirectly connected to the redox cores via C, N, O, S atoms, with zero or multiple, e.g., one, two, three, etc., methylene spacing groups.
[0073] Alternatively, or in addition, redox-active organic species of the invention may include groups which frustrate the oxygenation of the reduced state kinetically, e.g., by intramolecular and/or intermolecular non-covalent interactions including hydrogen bonding, zwitterionic interactions, and Lewis acid and base pair interactions to frustrate. The intramolecular non-covalent interactions may be introduced by covalently attaching functional groups to the redox cores. The intermolecular non-covalent interactions may be inter- or intramolecular interactions of functionalized redox molecules or may be provided by introducing additives into electrolytes (e.g., counterions to the negative charges on the reduced state which kinetically frustrate the reaction with oxygen). The additives could be bulky salts, including but not limited to tetraalkyl ammonium salts, such as tetramethyl ammonium, tetraethyl ammonium, tetrapropyl ammonium, tetrabutyl ammonium cations, etc. Corresponding anions before additive cations may include chloride, bromide, iodide, etc.
[0074] Exemplary electron withdrawing groups include NO.sub.2, CN, SO.sub.3R.sub.a, CHO, C(O)R.sub.a, C(O)O C(O)R.sub.a, C(O)OR.sub.a, (e.g., C(O)OH), CONH.sub.2, COO.sup., NR.sub.a3.sup.+, CF.sub.3, SO.sub.2R.sub.a, F, Cl, Br, I, OR.sub.a, SR.sub.a, P(O)(OR.sub.a).sub.2,(CH.sub.2).sub.1-3NO.sub.2, (CH.sub.2).sub.1-3CN, (CH.sub.2).sub.1-3SO.sub.3R.sub.a, (CH.sub.2).sub.1-3CHO, (CH.sub.2).sub.1-3C(O)R.sub.a, (CH.sub.2).sub.1-3C(O)OCOR.sub.a, (CH.sub.2).sub.1-3COOR.sub.a, (CH.sub.2).sub.1-3C(O)OH, (CH.sub.2).sub.1-3CONH.sub.2, (CH.sub.2).sub.1-3C(O)O, (CH.sub.2).sub.1-3NR.sub.a3.sup.+,(CH.sub.2).sub.1-3SO.sub.2R.sub.a, CH.sub.2CF.sub.3, CH.sub.2CCl.sub.3, CH.sub.2CBr.sub.3, CH.sub.2Cl.sub.3, CH.sub.2CHF.sub.2, CH.sub.2CHCl.sub.2, CH.sub.2CHBr.sub.2, CH.sub.2CHI.sub.2, CH.sub.2(CF.sub.2).sub.1-6CF.sub.3,(CH.sub.2).sub.1-3OR.sub.a, and (CH.sub.2).sub.1-3SR.sub.a, where each R.sub.a is independently H; optionally substituted C.sub.1-6 alkyl; optionally substituted C.sub.3-10 carbocyclyl; or optionally substituted C.sub.1-9 heterocyclyl having one to four heteroatoms independently selected from O, N, and S, e.g., SO.sub.3H, PO.sub.3H.sub.2, COOH, OH, NH.sub.2, N(CH.sub.3).sub.3.sup.+, NH.sub.3.sup.+, and ethyleneglycol (OCH.sub.2CH.sub.2OCH.sub.2CH.sub.2OH).
[0075] In some embodiments, the substituents are optionally substituted C.sub.1-6 alkyl groups including a quaternary ammonium group, optionally substituted C.sub.1-6 alkoxy groups including a quaternary ammonium group, optionally substituted C.sub.1-6 alkyl thio groups including a quaternary ammonium group. In some embodiments, the quaternary amine group is attached to a terminal carbon. In some embodiments, the one or more substituents include at least one (CH.sub.2).sub.nNR.sub.a3.sup.+ group, where n=2-11, where each R.sub.a is independently H; optionally substituted C.sub.1-6 alkyl; optionally substituted C.sub.3-10 carbocyclyl; optionally substituted C.sub.1-9 heterocyclyl having one to four heteroatoms independently selected from O, N, and S; optionally substituted C.sub.6-20 aryl; optionally substituted C.sub.1-9 heteroaryl having one to four heteroatoms independently selected from O, N, and S; or a nitrogen protecting group.
[0076] In some embodiments, the redox-active species is:
##STR00007## ##STR00008## ##STR00009## ##STR00010##
[0077] An example is bis-(trimethylammonio)propyl anthraquinone (BTMAPAQ)-based isomers. Our results indicate that the reduced states of BTMAPAQ isomers (with and without captured CO.sub.2) show excellent air-resistance, which is the key to be utilized for CO.sub.2 capture in air or flue gas. In some embodiments, the redox-active species is not a BTMAPAQ, e.g., is not 1,8-BTMAPAQ.
[0078] In some embodiments, at least 10%, e.g., at least 20, 30, 40, 50, 60, 70, 80, 90, 95, or 99%, of the reduced state is present after exposure to air for at least one day, e.g., at least 2, 3, 4, 5, 6, or 7 days or at least 1, 2, 3, or 4 weeks, or at least 1, 2, 3, 4, 5, or 6 months, e.g., the redox species is stable up to 6 months or one year.
Redox Inorganics
[0079] Inorganic redox-active species such as the nitrate (NO.sub.3.sup.)/nitrite (NO.sub.2.sup.) redox pair can be used to conduct PCET reaction. For example, the reduction of nitrate generates nitrite and hydroxide, increasing the solution pH:
NO.sub.3.sup.+H.sub.2O+2e.sup..fwdarw.NO.sub.2.sup.+20H.sup.
and the oxidation of nitrite generates nitrate and consumes hydroxide, decreasing the pH:
NO.sub.2.sup.+20H.sup..fwdarw.NO.sub.3.sup.+H.sub.2O+2e.sup.
[0080] Hence, the solution pH is reversibly tuned, which is followed by reversible CO.sub.2 capture/release. The redox potential of the pair is 0.94 V vs. RHE (S. Bratsch, J. Phys. Chem. Ref. Data 1989, 18, 1). This redox potential is higher than most ROs, whose redox potentials are usually around 0-0.2 V. vs RHE depends on the pH. As a result, the reduced form of the nitrate/nitrite pair, i.e., NO.sub.2.sup., is much more air-stable compared to the reduced form of ROs. The superior air-stability of NO.sub.2 at pH >6 is known (W. Braida et al., Water, Air and Soil Pollution 2000, 118, 13-26). Besides the air stability, the high solubility of nitrate and nitrite salts (>10 M) and their low price ($400-600/MT or $0.5-1/KAh, about two orders of magnitude smaller than the lower end of RO price, i.e., $84) makes the redox pair advantageous for DAC and flue gas capture. The high overpotential of the nitrate reduction and nitrite oxidation processes can be mediated with metal-based catalysts, enzymes or modified electrodes (Z. Mumtarin et al., Electrochimica Acta 2020, 346, 135994; G. Mersal et al., Int. J. Electrochem. Sci. 2011, 6, 761-777; J. Craig et al., J. Am. Chem. Soc. 1989, 111, 2111-2115; J. Jiang et al., Inorg. Chem. 2005, 44, 1068-10725. F. Armijo et al., Journal of Molecular Catalysis A; Chemical 2007, 148-154; A. Chamsi et al., Analyst 1988, 133, 1723-1727). The long-term stability of nitrite, which suffers from possible disproportionation reaction if nitrite is protonated:
3HNO.sub.2.fwdarw.HNO.sub.3+2NO(g)+H.sub.2O
is handled by carefully maintaining the pH at above 5.3, where >99% of nitrite molecules are deprotonated, and by keeping a high concentration of NO.sub.3.sup. (W. Braida et al., Water, Air and Soil Pollution 2000, 118, 13-26).
Capture Devices
[0081] Capture devices may include a negolyte (negative electrolyte) that includes, e.g., a RO or RI dissolved or suspended in aqueous solution; a posolyte (positive electrolyte) that includes, e.g., a redox-active species; and a barrier separating the two. The redox-active species in negolyte and posolyte could be either the same molecule or different molecules. The device further includes at least two electrodes, one in contract with the negolyte and one in contact with the posolyte. The electrodes may be carbon-based materials, pure metals, or alloys. Electrodes may be doped or decorated with catalysts.
[0082] During invasion, the high-pH liquid may be sprayed down through a solid lattice, providing a liquid/gas interface for CO.sub.2 in the gas to enter the liquid. A similar lattice may be employed when CO.sub.2 gas is released from the liquid.
[0083] The devices may also employ redox species having an aminoxyl radical group, e.g., 2,2,6,6-tetramethylpiperidine-N-oxyl (TEMPO) or substituted versions thereof (e.g., substituted like a heterocycle as described herein). Devices may also include aminoxyl radical species as catalysts/charge mediators, e.g., compounds such as (4-hydroxy-2,2,6,6-tetramethylpiperidin-1-yl)oxyl (TEMPO), 1-hydroxy-2,2,6,6-tetramethylpiperidine (TEMPOH), 4-oxo-2,2,6,6-tetramethyl-1-piperidinyloxy, 4-acetamido-2,2,6,6-tetramethylpiperidine 1-oxyl, 4-carboxy-2,2,6,6-tetramethylpiperidine 1-oxyl, 4-Amino-2,2,6,6-tetramethylpiperidine-1-oxyl, etc.). Compounds having a phthalimido-N-oxyl radical group (e.g., N-phthalimido-N-oxyl (PINO)) may also be used. Such species may be employed to capture CO.sub.2 on the positive or negative side of the device.
[0084] Examples of redox-active species for the posolyte include bromine, chlorine, iodine, vanadium, chromium, cobalt, iron (e.g., ferricyanide/ferrocyanide or a ferrocene derivative, e.g., as described in WO 2018/032003), aluminum, e.g., aluminum(III) biscitrate monocatecholate, manganese, cobalt, nickel, copper, or lead, e.g., a manganese oxide, a cobalt oxide, or a lead oxide. A benzoquinone may also be used as the second redox-active species. Other redox-active species suitable for use in batteries of the invention are described in WO 2014/052682, WO 2015/048550, WO 2016/144909, and WO 2020/072406, the redox-active species of which are incorporated by reference. The redox-active species may be dissolved or suspended in solution (such as aqueous solution) or be in the solid state.
[0085] Posolyte and negolyte may include the same redox species but with the opposite states, e.g., one is the reduced state, and the other one is the oxidized state. One side is to capture CO.sub.2, e.g., from flue gas or air, and the other side is to release CO.sub.2.
[0086] In some embodiments, the electrolytes are both aqueous, where the negolyte and posolyte are aqueous.
[0087] In addition, the electrolyte may include other solutes, e.g., acids (e.g., HCl) or bases (e.g., LiOH, NH.sub.4OH, NaOH, or KOH) or alcohols (e.g., methyl, ethyl, or propyl) and other co-solvents to increase the solubility of a particular species, e.g., quinone/hydroquinone. Counter ions, such as cations, e.g., NH.sub.4.sup.+, Li.sup.+, Na.sup.+, K.sup.+, or a mixture thereof, may also be present. In certain embodiments, the pH of one or both of the electrolytes may be >7, e.g., at least 8, 9, 10, 11, 12, 13, or 14, 8-14, 9-14, 10-14, 11-14, 12-14, 13-14, or about 14. In certain embodiments, the pH of one or both of the electrolytes may be <7, e.g., at less than 7, 6, 5, 4, 3, 2, or 1, e.g., 7-1, 7-5, 6-4, 5-2, 3-1, 2-1, or about 1. The pH may be less than 1. The pH may be a negative pH. The electrolyte may or may not be buffered to maintain a specified pH. In methods and systems using nitrite ions, the pH may be modulated to remain above pH 7 to prevent unwanted side reactions of the protonated nitrite ion. The concentration of the negolyte and posolyte will be suitable to operate the device, e.g., battery or carbon capture device, for example, from 0.1-15 M, or from 0.1-10 M. In some embodiments, the solution is at least 10%, 20%, 30%, 40%, 50%, 60%, 70%, or 80% water, by mass. The electrolytes may contain one or more redox-active species (e.g., ROs or RIs) that act as redox mediators.
[0088] In addition to water, solutions or suspensions may include alcohols (e.g., methyl, ethyl, or propyl) and other co-solvents to increase the solubility of a particular species. In some embodiments, the solution or suspension is at least 10%, 20%, 30%, 40%, 50%, 60%, 70%, or 80% water, by mass. Alcohol or other co-solvents may be present in an amount required to result in a particular concentration of species. The pH of the aqueous solution or suspension may also be adjusted by addition of acid or base, e.g., to aid in solubilizing a species.
[0089] The barrier allows the passage of ions, such as sodium or potassium, but not a significant amount of the redox-active species. Examples of ion conducting barriers are NAFION, i.e., sulfonated tetrafluoroethylene based fluoropolymer-copolymer, FUMASEP, i.e., non-fluorinated, sulfonated polyaryletherketone-copolymer, e.g., FUMASEP E-620(K), hydrocarbons, e.g., polyethylene, and size exclusion barriers, e.g., ultrafiltration or dialysis membranes with a molecular weight cut off of 100, 250, 500, or 1,000 Da. Examples of membranes include Selemion DSV and Selemion AMV. For size exclusion membranes, the required molecular weight cut off is determined based on the molecular weight of the negolytes and posolytes employed. Porous physical barriers may also be included, e.g., when the passage of redox-active species is tolerable. A redox flow cell may have two barriers and a central compartment disposed therebetween.
[0090] Electrodes for use with batteries and CO.sub.2 capture devices may include any carbon electrode, e.g., glassy carbon electrodes, carbon paper electrodes, carbon felt electrodes, or carbon nanotube electrodes. Titanium electrodes may also be employed. Electrodes can also be made of a high specific surface area conducting material, such as a nanoporous metal sponge (T. Wada, A. D. Setyawan, K. Yubuta, and H. Kato, Scripta Materialia 65, 532 (2011)), which has been synthesized previously by electrochemical dealloying (J. D. Erlebacher, M. J. Aziz, A. Karma, N. Dmitrov, and K. Sieradzki, Nature 410, 450 (2001)), or a conducting metal oxide, which has been synthesized by wet chemical methods (B. T. Huskinson, J. S. Rugolo, S. K. Mondal, and M. J. Aziz, arXiv:1206.2883 [cond-mat.mtrl-sci]; Energy & Environmental Science 5, 8690 (2012); S. K. Mondal, J. S. Rugolo, and M. J. Aziz, Mater. Res. Soc. Symp. Proc. 1311, GG10.9 (2010)). Chemical vapor deposition can be used for conformal coatings of complex 3D electrode geometries by ultra-thin electrocatalyst or protective films. Other electrodes are known in the art.
[0091] A carbon capture device may include additional components as is known in the art. Negolytes and posolytes may be housed in a suitable reservoir. A carbon capture device may further include one or more pumps to pump aqueous solutions or suspensions past one or both electrodes. Alternatively, the electrodes may be placed in a reservoir that is stirred or in which the solution or suspension is recirculated by any other method, e.g., convection, sonication, etc. A carbon capture device may also include graphite flow plates and corrosion-resistant metal current collectors.
[0092] The balance of the system around the cell includes fluid handling and storage, and voltage and round-trip energy efficiency measurements can be made. Systems configured for measurement of negolyte and posolyte flows and pH, pressure, temperature, current density and cell voltage may be included and used to evaluate cells, e.g., to determine when to apply the electrical pulse. Fluid sample ports can be provided to permit sampling of both electrolytes, which will allow for the evaluation of parasitic losses due to reactant crossover or side reactions. Electrolytes can be sampled and analyzed with standard techniques.
[0093] Suitable cells, electrodes, membranes, and pumps for redox flow batteries are known in the art, e.g., WO 2014/052682, WO 2015/048550, WO 2016/144909, and WO 2020/072406, the battery components of which are hereby incorporated by reference.
Methods
[0094] Solutions of oxygen-resistant redox-active species are used to capture CO.sub.2, e.g., from air or flue gas and release pure CO.sub.2.
[0095] The methods include providing an electrochemical cell including a redox-active species dissolved or dispersed in aqueous solution. The redox-active species is electrochemically reduced to a reduced state. The reduced state is then contacted with a mixture of gases including CO.sub.2, e.g., by bubbling air or flue gas through an aqueous solution. Air is present in the mixture of gases, which would typically oxidize a reduced state of the redox-active species back to the oxidized state, but these undesired reactions are prevented or slowed using redox-active species that are resistant to oxidation in their reduced states. The reduction of the redox-active species may generate hydroxide ions which react with CO.sub.2 to form inorganic carbonates (PCET), and/or the reduced state may itself react (e.g., by a nucleophilic addition reaction) with CO.sub.2 to form a CO.sub.2 adduct (
[0096]
[0097] The invention can be used for an electrochemical CO.sub.2 capture system, e.g., employing proton-coupled redox-active species 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 CO.sub.2. The CO.sub.2 capture device can be used to sequester gaseous CO.sub.2 from a point source, such as flue gas, or from ambient air. The total possible amount of sequestered carbon, the Dissolved Inorganic Carbon (DIC), depends on the partial pressure of CO.sub.2 above the aqueous solution or aqueous suspension, and the pH determines the form of the carbon, e.g., dissolved CO.sub.2, HCO.sub.3 or CO.sub.3.sup.2. CO.sub.2 can be captured from a gaseous source, e.g., point sources or ambient air, by dissolving into an aqueous solution. More CO.sub.2 can be dissolved as the pH of the aqueous solution or aqueous suspension increases, resulting in the conversion of CO.sub.2 into HCO.sub.3.sup. or CO.sub.3.sup.2 ions. More CO.sub.2 can be dissolved in an aqueous solution or aqueous suspension as HCO.sub.3 or CO.sub.3.sup.2 than CO.sub.2, resulting in supersaturation of CO.sub.2 in the aqueous solution or aqueous suspension. Once captured, the CO.sub.2 can be released by acidifying the aqueous solution or aqueous suspension, e.g., by electrochemical oxidation. Alternatively, the reduced state may react directly with CO.sub.2to produce an adduct, and the CO.sub.2 can subsequently be released by oxidizing the adduct. In principle, the pure CO.sub.2 obtained after separation can be converted back into useful chemical fuels and feedstocks with carbon-free energy, thus providing fuels and feedstocks without added CO.sub.2 emissions.
EXAMPLES
[0098] The invention will be further described by the following non-limiting examples.
Example 1: Reduced 1,8-BTMAPAQ with Captured CO.SUB.2 .Can Withstand the Presence of Air for 5 Days
[0099] We first prepared the reduced 1,8-BTMAPAQ with captured CO.sub.2 sample in D.sub.2O in the presence of 1 M tetrabutylammonium bromide (TBABr). As we intentionally exposed the solution to air over nine days, we tracked its .sup.1H NMR spectra, which provides precise information about the bonding environment of the hydrogen atoms in molecules. As shown in
Example 2: Reduced 1,4-BTMAPAQ with and without Captured CO.SUB.2
[0100] We prepared the reduced 1,4-BTMAPAQ sample in D.sub.2O in the presence of 1 M KCl. As we intentionally exposed the solution to air over six days, we tracked its .sup.1H NMR spectra, which provides precise information about the bonding environment of the hydrogen atoms in molecules. As shown in
[0101] We prepared the reduced 1,4-BTMAPAQ with captured CO.sub.2 sample in D.sub.2O in the presence of 1 M KCl. As we intentionally exposed the solution to air over six days, we tracked its .sup.1H NMR spectra, which provides precise information about the bonding environment of the hydrogen atoms in molecules. As shown in
Example 3: Reduced 1,5-BTMAPAQ with and without Captured CO.SUB.2
[0102] We prepared the reduced 1,5-BTMAPAQ sample in D.sub.2O in the presence of 1 M KCl. As we intentionally exposed the solution to air over six days, we tracked its .sup.1H NMR spectra, which provides precise information about the bonding environment of the hydrogen atoms in molecules. As shown in
[0103] We prepared the reduced 1,5-BTMAPAQ with captured CO.sub.2 sample in D.sub.2O in the presence of 1 M KCl. As we intentionally exposed the solution to air over six days, we tracked its .sup.1H NMR spectra, which provides precise information about the bonding environment of the hydrogen atoms in molecules. As shown in
Preparation of the Reduced BTMAPAQ Isomer Samples First, 0.1 M BTMAPAQ isomers were dissolved in D.sub.2O, 0.1 M sodium dithionite (Na.sub.2S.sub.2O.sub.4) was added into the solutions to chemically reduce BTMAPAQ. At pH=7, the potential of Na.sub.2S.sub.2O.sub.4 is 0.66 V vs. SHE, which is lower than the reduction potential of BTMAPAQ (0.41 V vs. SHE). Therefore, Na.sub.2S.sub.2O.sub.4 is chosen for the chemical reduction. The redox occurs with formation of sulfite and protons, S.sub.2O.sub.4.sup.2+2H.sub.2O .fwdarw.2 HSO.sub.3.sup.+2 e.sup.+2 H.sup.+. To avoid the pH change while introducing Na.sub.2S.sub.2O.sub.4, 0.2 M of KOH was added in advance to neutralize the produced protons. The solutions were immediately transferred to NMR tubes. For 1,8-BTMAPAQ, 1 M TBABr was added as the supporting salt additive, for 1,4- and 1,5-BTMAPAQ isomers, 1 M KCl was added as the supporting salt additive.
[0104] Preparation of the reduced BTMAPAQ isomer with captured CO.sub.2 samples 0.1 M BTMAPAQ isomers were dissolved in D.sub.2O, 0.1 M sodium dithionite (Na.sub.2S.sub.2O.sub.4) was added into the solutions to chemically reduce BTMAPAQ, 0.2 M of KOH was added in advance to neutralize the produced protons. The solutions were immediately transferred to NMR tubes, and excess dry ice particulates were added to the tube to form organic carbonates.
1,8-BTMAPAQ-Based CO.SUB.2 .Capture Experiment Procedures:
[0105] 1. To a 50 ml three-neck flask, 0.5 mmol Na.sub.2S.sub.2O.sub.4, 1.2 mmol KOH were added and purged with N2 for 30 mins. [0106] 2. 5 ml 0.1 M 1,8-BTMAP-AQ (0.5 mmol) in 1 M TBABr was injected to the flask for chemical reduction. (S.sub.2O.sub.4.sup.2+2 OH.sup..fwdarw.2 HSO.sub.3.sup.+2 e.sup.; Q+2 e.sup..fwdarw.Q.sup.2) [0107] 3. The solution was then bubbled with CO.sub.2 for 15 mins for quinone+CO.sub.2 adduct formation.
Q.sup.2+2 CO.sub.2.fwdarw.Q(CO.sub.2).sub.2.sup.2 [0108] The adduct solution was purged with N2 for 15 mins to remove the headspace CO.sub.2. [0109] The adduct solution was exposed to air with rigorous stirring for 15 mins to examine the air stability of the water-soluble organic carbonate [Q(CO.sub.2).sub.2.sup.2], then the solution was purged with N2 for 5 mins to remove residual air. [0110] 4. The three-neck flask was connected to a flask containing 500 mL saturated Ba(OH).sub.2 solution with a double-ended needle. A N2-filled balloon was connected to the three-neck flask. [0111] 5. 2 ml 0.5 M potassium ferricyanide (1 mmol) solution was injected to the solution, and the generated CO.sub.2 was transferred to Ba(OH).sub.2 solution by the N2 carrier gas.
2 Fe(CN).sub.6.sup.3+Q(CO.sub.2).sub.2.sup.2.fwdarw.2 Fe(CN).sub.6.sup.4+Q+CO.sub.2 (g)
CO.sub.2+Ba(OH).sub.2.fwdarw.BaCO.sub.3 (s)+H.sub.2O [0112] 6. The BaCO.sub.3 suspensions were centrifugated and the solids were dried in a convection oven for 3 days, the products were weighed for 3 times until the mass did not change at all.
[0113] Each quinone can capture 2 CO.sub.2 molecules. For example, 0.5 mmol 1,8-BTMPAQ may capture up to 1 mmol CO.sub.2, leading to the precipitation of 1 mmol BaCO.sub.3, i.e., 197 mg of BaCO.sub.3 when CO.sub.2 is released into Ba(OH).sub.2 solution. In this example, 200 mg BaCO.sub.3 was captured in N2; and 170 mg BaCO.sub.3 was captured when the solution with captured CO.sub.2 was vigorously stirred in air. That is 1.7 CO.sub.2 molecules per BTMPAQ were captured per quinone with air exposure, 0.3 CO.sub.2 per 1,8-BTMPAQ escaped during the air exposure.
Example 4
[0114] We prepared the reduced 2,7-BTMAPFL sample, i.e., 2,7-BTMAPFL-OH, in D.sub.2O in the presence of 1 M KCl at pH 7. We vigorously stirred the solution in air for 12 hours, then checked its .sup.1H NMR spectra before and after being stirred in air. As shown in
[0115] The 2,7-BTMAPFL molecule undergoes PCET process and forms 2,7-BTMAPFL-OH after the electrochemical reduction; meanwhile, the electrolyte pH swings from near neutral (7) to 14. Therefore, we also investigated the air stability of 2,7-BTMAPFL-OH at pH 14 by vigorously stirring the pH 14 solution in air for 12 hours. As shown in
[0116] The cyclic voltammetry experiments are shown in
[0117] Other embodiments are in the claims.