Method, device and fuel for hydrogen generation
A method and a device for generating of hydrogen are provided with which an instantaneous release of hydrogen in considerable amounts is possible. The method comprises a one or two step mixing including injecting the fuel and an activator fluid into a reaction chamber. The device is adapted to be operated with such a method. Further, a fuel suitable for the use with such a method is provided, the fuel being based on a dry metal hydride or a dry metal borohydride being dispersed in a non-aqueous dispersion medium. Moreover, a method for (re-) fueling the hydrogen generating device at a service station and a method for supplying a service station with fuel are provided.
1. A method for generating hydrogen, H 2 , comprising the steps of:
a) providing a metal borohydride, M(BH 4 ) x , as a hydrogen carrier, wherein M is a metal and x denotes a valence value of the metal;
b) providing water having a conductance value below 0.5 μS as an activator fluid;
c) bringing the hydrogen carrier and the activator fluid together and allowing the hydrogen carrier and the activator fluid to react to provide hydrogen, H 2 .
2. The method according to claim 1 , wherein the hydrogen carrier is provided in a hydrogen carrier fluid comprising molecules or particles of the hydrogen carrier dissolved or dispersed in an inert fluid medium.
3. The method according to claim 2 , wherein the hydrogen carrier fluid and the activator fluid are injected into a reaction chamber, and the hydrogen carrier fluid and the activator fluid are injected into the reaction chamber in order to cause an intensive mixing of the molecules or particles of the hydrogen carrier with the activator fluid.
4. The method according to claim 3 , wherein the hydrogen carrier fluid and the activator fluid are injected under high pressure.
5. The method according to claim 2 , wherein a particle size of particles of the hydrogen carrier is 10 microns or smaller.
6. The method according to claim 2 , wherein a particle size of particles of the hydrogen carrier is about 1 micron or smaller.
7. The method according to claim 2 , wherein the inert fluid medium is a fluid or a combination of fluids selected from the group consisting of mineral oils, copolymers of ethylene and propylene, poly(alpha)olefins and ether alkoxylates.
8. The method according to claim 2 , wherein a concentration of molecules of the hydrogen carrier in the inert fluid medium is at least 60%.
9. The method according to claim 2 , wherein a concentration of molecules of the hydrogen carrier in the inert fluid medium is within the range of 70% to 75%.
10. The method according to claim 2 , wherein a viscosity of the hydrogen carrier fluid is 1 to 50 times that of water at room temperature.
11. The method according to claim 2 , wherein a viscosity of the hydrogen carrier fluid is 1 to 2 times that of water at room temperature.
12. The method according to claim 1 , wherein the metal, M, of the hydrogen carrier is selected from the group consisting of Li, Na, Be, Mg, Ca and Al.
13. The method according to claim 1 , wherein the hydrogen carrier comprises Na(BH 4 ) 2 , Ca(BH 4 ) 2 and/or Al(BH 4 ) 3 .
14. The method according to claim 1 , wherein the water is purified, demineralised, treated with reverse osmosis and/or filtered by an electrostatic filter.
15. The method according to claim 1 , wherein the water is recycled water from a fuel cell.
16. A binary fuel for generating hydrogen, H 2 , comprising a metal borohydride, M(BH 4 ) x , as a hydrogen carrier and water having a conductance value below 0.5 μS as an activator fluid, wherein M is a metal and x denotes a valence value of the metal.
17. The fuel according to claim 16 , wherein the hydrogen carrier is provided in a hydrogen carrier fluid comprising molecules or particles of the hydrogen carrier dissolved or dispersed in an inert fluid medium.
18. The fuel according to claim 17 , wherein a particle size of particles of the hydrogen carrier is 10 microns or smaller.
19. The fuel according to claim 17 , wherein a particle size of particles of the hydrogen carrier is about 1 micron or smaller.
20. The fuel according to claim 17 , wherein the inert fluid medium is a fluid or a combination of fluids selected from the group consisting of mineral oils, copolymers of ethylene and propylene, poly(alpha)olefins and ether alkoxylates.
21. The fuel according to claim 17 , wherein a concentration of molecules of the hydrogen carrier in the inert fluid medium is at least 60%.
22. The fuel according to claim 17 , wherein a concentration of molecules of the hydrogen carrier in the inert fluid medium is within the range of 70% to 75%.
23. The fuel according to claim 17 , wherein the viscosity of the hydrogen carrier fluid is from 1 to 50 times that of water at room temperature.
24. The fuel according to claim 17 , wherein the viscosity of the hydrogen carrier fluid is 1 to 2 times that of water at room temperature.
25. The fuel according to claim 16 , wherein the metal, M, of the hydrogen carrier is selected from the group consisting of Li, Na, Be, Mg, Ca and Al.
26. The fuel according to claim 16 , wherein the hydrogen carrier comprises Na(BH 4 ) 2 , Ca(BH 4 ) 2 and/or Al(BH 4 ) 3 .