Solar power for thermochemical production of hydrogen
View Patent ↗A solar-powered hydrogen production system includes a thermochemical system and solar heating system. The thermochemical system produces hydrogen. The solar heating system has a molten salt heat transfer medium for providing thermal energy to the thermochemical system.
1. A solar-powered hydrogen production system, the system comprising:
a low temperature thermochemical system using a copper chloride thermochemical cycle for producing hydrogen with a maximum reaction temperature of about 530° C.; and
a solar heating system having a molten salt heat transfer medium for providing thermal energy to the thermochemical system;
wherein the copper chloride thermochemical cycle for producing hydrogen comprises the following set of chemical reactions and reaction temperatures:
2Cu(s)+2HCl(l)=2CuCl(l)+H 2 (g) at a temperature of between about 430° C. to about 475° C.;
2CuCl(s)=2CuCl 2 (aq)+2Cu at a temperature of between about 25° C. to about 75° C.;
2CuCl 2 (s)+H 2 O(g)=CuO*CuCl 2 (s)+2HCl(g) at a temperature of between about 350° C. to 400° C.; and
CuO*CuCl 2 (s)=2CuCl(l)+½O 2 (g) at a temperature of about 530° C.
2. The solar-powered hydrogen production system of claim 1 , wherein the molten salt heat transfer medium comprises about 60% sodium nitrate and about 40% potassium nitrate.
3. The solar-powered hydrogen production system of claim 1 , wherein the solar heating system provides thermal energy for generating electrical energy that is supplied to the thermochemical system.
4. The solar-powered hydrogen production system of claim 3 , wherein the thermochemical system also produces oxygen.
5. A system comprising:
a low temperature thermochemical system using a copper chloride thermochemical cycle for producing hydrogen with a maximum reaction temperature of about 530° C.;
a molten salt heat transfer medium for providing thermal energy to the low temperature thermochemical system; and
a solar receiver for heating the heat transfer medium;
wherein the copper chloride thermochemical cycle for producing hydrogen comprises the following set of chemical reactions and reaction temperatures:
2Cu(s)+2HCl(l)=2CuCl(l)+H 2 (g) at a temperature of between about 430° C. to about 475° C.;
2CuCl(s)=2CuCl 2 (aq)+2Cu at a temperature of between about 25° C. to about 75° C.;
2CuCl 2 (s)+H 2 O(g)=CuO*CuCl 2 (s)+2HCl(g) at a temperature of between about 350° C. to 400° C.; and
CuO*CuCl 2 (s)=2CuCl(l)+½O 2 (g) at a temperature of about 530° C.
6. The system of claim 5 , wherein the heat transfer medium comprises molten salt.
7. The system of claim 6 , wherein the molten salt comprises about 60% sodium nitrate and about 40% potassium nitrate.
8. The system of claim 6 , wherein the heat transfer medium provides thermal energy to the thermochemical process.
9. The system of claim 6 , wherein the heat transfer medium is used to generate electrical energy for use in the thermochemical process.
10. The system of claim 6 , wherein the system is a solar heating system.
11. A method comprising:
capturing solar energy from sunlight;
heating a heat transfer medium with the solar energy;
transporting the heat transfer medium to a hydrogen and oxygen production system; and
generating hydrogen and oxygen with the hydrogen and oxygen production system with a maximum reaction temperature of about 530° C.; wherein the hydrogen and oxygen production system is a copper chloride thermochemical cycle comprising the following set of chemical reactions and reaction temperatures:
2Cu(s)+2HCl(l)=2CuCl(l)+H 2 (g) at a temperature of between about 430° C. to about 475° C.;
2CuCl(s)=2CuCl 2 (aq)+2Cu at a temperature of between about 25° C. to about 75° C.;
2CuCl 2 (s)+H 2 O(g)=CuO*CuCl 2 (s)+2HCl(g) at a temperature of between about 350° C. to 400° C.; and
CuO*CuCl 2 (s)=2CuCl(l)+½O 2 (g) at a temperature of about 530° C.
12. The method of claim 11 , wherein capturing solar energy comprises using a solar heating system.
13. The method of claim 11 , wherein the heat transfer medium comprises molten salt.
14. The method of claim 13 , wherein the molten salt comprises about 60% sodium nitrate and about 40% potassium nitrate.
15. The method of claim 13 , wherein transporting the molten salt to the low temperature hydrogen and oxygen production system comprises providing at least one of thermal energy and electrical energy to the hydrogen and oxygen production system.
16. The method of claim 11 , wherein the heat transfer medium provides thermal energy to the hydrogen and oxygen production system.