Solar fuels generator with pH separation
A solar fuels generator includes an anolyte and a catholyte in contact with a separator. The separator is configured such that the pH of the anolyte and the pH of the catholyte are each held at a steady state pH level during operation of the solar fuels generator. The steady state pH level of the anolyte is different from the steady state pH level of the catholyte.
1. A solar fuels generator, comprising:
an anolyte reservoir;
a catholyte reservoir,
a anode in the anolyte reservoir,
a photocathode in the catholyte reservoir,
a separator between the anolyte reservoir and catholyte reservoir,
an anolyte in the anolyte reservoir in contact with the separator and the anode, and
a catholyte in the catholyte reservoir in contact with the separator and the photocathode,
a pH of the anolyte being at a steady state pH level during operation of the solar fuels generator and a pH of the catholyte being at a steady state pH level during operation of the solar fuels generator, and
the steady state pH level of the anolyte being different from the steady state pH level of the catholyte.
2. The generator of claim 1 , wherein water dissociates in the separator during the operation of the solar fuels generator.
3. The generator of claim 1 , wherein hydroxide anions enter the anolyte from the separator during operation of the solar fuels generator and protons enter catholyte from the separator during operation of the solar fuels generator.
4. The generator of claim 1 , wherein the solar fuels generator provides a solar-to-fuel (STF) conversion efficiency above 9% during operation of the solar fuels generator.
5. The generator of claim 1 , wherein an absolute value of a difference between the steady state pH level of the anolyte and the steady state pH level of the catholyte is more than 5.
6. The generator of claim 1 , wherein the separator includes an anion exchange membrane and a cation exchange membrane arranged such that a component of the anolyte and/or the catholyte cannot travel across the separator without traveling through both the anion exchange membrane and the cation exchange membrane.
7. The generator of claim 6 , wherein the anion exchange membrane includes a polymer functionalized with quaternary ammonium groups and the cation exchange membrane includes a material selected from the group consisting of polyaromatic polymers and fluorinated polymers functionalized with sulfonic acid groups.
8. The generator of claim 6 , wherein a catalyst is positioned between the anion exchange membrane and the cation exchange membrane.
9. The generator of claim 8 , wherein the catalyst is selected to catalyze water dissociation.
10. The generator of claim 8 , wherein the catalyst is selected from the group consisting of TiOH, ZrOH, SiOH, poly(ferrocenyldimethysilane), poly(acrylamide), graphene and graphene oxide.
11. A solar fuels generator, comprising:
a first reactor configured to contain an anolyte in contact with a separator and an anode and a second reactor configured to contain a catholyte in contact with the separator and a photocathode, and
the separator includes an anion exchange membrane and a cation exchange membrane arranged such that a component of the anolyte and/or the catholyte cannot travel across through the separator without traveling through both the anion exchange membrane and the cation exchange membrane.
12. A solar fuels generator, comprising:
a first reactor configured to contain an anolyte in contact with a separator and an anode and a second reactor configured to contain a catholyte in contact with the separator and a photocathode,
the separator being configured to keep a pH of the anolyte at a steady state pH level during operation of the solar fuels generator and to keep a pH of the anolyte at a steady state pH level during operation of the solar fuels generator, and
the steady state pH level of the anolyte being different from the steady state pH level of the catholyte.
13. The generator of claim 12 , wherein the separator is configured such that water dissociates inside of the separator during the operation of the solar fuels generator.
14. The generator of claim 12 , wherein the separator is configured such that hydroxide anions enter the anolyte from the separator during operation of the solar fuels generator and protons enter catholyte from the separator during operation of the solar fuels generator.
15. The generator of claim 12 , wherein an absolute value of a difference between the steady state pH level of the anolyte being and the different from the steady state pH level of the catholyte is more than 5.
16. The generator of claim 12 , wherein the separator includes an anion exchange membrane and a cation exchange membrane arranged such that a component of the anolyte and/or the catholyte cannot travel across through the separator without traveling through both the anion exchange membrane and the cation exchange membrane.
17. The generator of claim 16 , wherein the anion exchange membrane includes a polymer functionalized with quaternary ammonium groups and the cation exchange membrane includes a material selected from the group consisting of polyaromatic polymers and fluorinated polymers functionalized with sulfonic acid groups.
18. The generator of claim 16 , wherein a catalyst is positioned between the anion exchange membrane and the cation exchange membrane.
19. The generator of claim 18 , wherein the catalyst is selected to catalyze water dissociation.
20. The generator of claim 18 , wherein the catalyst is selected from the group consisting of TiOH, ZrOH, SiOH, poly(ferrocenyldimethysilane), poly(acrylamide), graphene and graphene oxide.