Reactor with advanced architecture for the electrochemical reaction of CO2, CO and other chemical compounds
A platform technology that uses a novel membrane electrode assembly, including a cathode layer, an anode layer, a membrane layer arranged between the cathode layer and the anode layer, the membrane conductively connecting the cathode layer and the anode layer, in a CO x reduction reactor has been developed. The reactor can be used to synthesize a broad range of carbon-based compounds from carbon dioxide and other gases containing carbon.
1. A membrane electrode assembly comprising:
a cathode layer comprising a reduction catalyst;
an anode layer comprising an oxidation catalyst;
a membrane layer comprising a first cation-conducting polymer, the membrane layer arranged between the cathode layer and the anode layer, the membrane layer conductively connecting the cathode layer and the anode layer; and
a cathode buffer layer comprising a first anion-conducting polymer, wherein the cathode buffer layer is arranged between the cathode layer and the membrane layer and conductively connects the cathode layer and the membrane layer, wherein the cathode buffer layer is porous such that gas can be transported in the cathode buffer layer and wherein the membrane layer is non-porous such that gas is prevented from passing between the cathode layer and the anode layer.
2. The membrane electrode assembly of claim 1 , further comprising an anode buffer layer, comprising a second cation-conducting polymer, arranged between the membrane layer and the anode layer.
3. The membrane electrode assembly of claim 2 , wherein the first and second cation-conducting polymers comprise a perfluorosulfonic acid (PFSA) polymer, and wherein the anode buffer layer is porous.
4. The membrane electrode assembly of claim 1 , wherein the cathode buffer layer further comprises inert filler particles that form a porosity of the cathode buffer layer.
5. The membrane electrode assembly of claim 4 , wherein the inert filler particles comprise at least one of diamond particles, boron-doped diamond particles, polyvinylidene difluoride (PVDF) particles, and polytetrafluoroethylene (PTFE) particles.
6. The membrane electrode assembly of claim 5 , wherein a size of each of the inert filler particles is between about 10 nanometers and about 200 nanometers.
7. The membrane electrode assembly of claim 1 , wherein the first anion-conducting polymer is selected from a group consisting of Sustainion, FumaSep FAA-3, and Tokuyama anion exchange polymer.
8. The membrane electrode assembly of claim 1 , wherein the cathode layer further comprises a second anion-conducting polymer.
9. The membrane electrode assembly of claim 8 , wherein the first anion-conducting polymer and the second anion-conducting polymer are the same polymer.
10. The membrane electrode assembly of claim 8 , wherein the first anion-conducting polymer and the second anion-conducting polymer are Sustainion.
11. The membrane electrode assembly of claim 1 , wherein the anode layer further comprises a second cation-conducting polymer.
12. The membrane electrode assembly of claim 11 , wherein the first cation-conducting polymer and the second cation-conducting polymer are the same polymer.
13. The membrane electrode assembly of claim 1 , wherein the thickness of the cathode buffer layer is between 200 nm and 100 μm.
14. The membrane electrode assembly of claim 1 , wherein the cathode buffer layer has a porosity between 0.1% and 95%.
15. A CO x reduction reactor comprising:
a membrane electrode assembly comprising:
a cathode layer comprising a reduction catalyst;
an anode layer comprising an oxidation catalyst;
a membrane layer comprising a first cation-conducting polymer, the membrane layer arranged between the cathode layer and the anode layer, the membrane layer conductively connecting the cathode layer and the anode layer; and
a cathode buffer layer comprising a first anion-conducting polymer, wherein the cathode buffer layer is arranged between the cathode layer and the membrane layer and conductively connects the cathode layer and the membrane layer, wherein the cathode buffer layer is porous such that gas can be transported in the cathode buffer layer and wherein the membrane layer is non-porous such that gas is prevented from passing between the cathode layer and the anode layer;
a cathode manifold coupled to the cathode layer; and
an anode manifold coupled to the anode layer.
16. The CO x reduction reactor of claim 15 , wherein the cathode manifold comprises a cathode support structure adjacent to the cathode layer, the cathode support structure comprising:
a cathode polar plate;
a cathode gas diffusion layer arranged between the cathode polar plate and the cathode layer;
a first inlet fluidly connected to the cathode gas diffusion layer; and
a first outlet fluidly connected to the cathode gas diffusion layer; and
wherein the anode manifold comprises an anode support structure adjacent to the anode layer, the anode support structure comprising:
an anode polar plate;
an anode gas diffusion layer arranged between the anode polar plate and the anode layer;
a second inlet fluidly connected to the anode gas diffusion layer; and
a second outlet fluidly connected to the anode gas diffusion layer.
17. The CO x reduction reactor of claim 15 , wherein the cathode layer further comprises a second anion-conducting polymer.
18. The CO x reduction reactor of claim 15 , wherein the anode layer further comprises a second cation-conducting polymer.
19. The CO x reduction reactor of claim 15 , wherein the thickness of the cathode buffer layer is between 200 nm and 100 μm.
20. The CO x reduction reactor of claim 15 , wherein the cathode buffer layer has a porosity between 0.1% and 95%.