Method, device and fuel for hydrogen generation

• US 8,636,975 B2
• Filed: 01/27/2010
• Issued: 01/28/2014
• Est. Priority Date: 01/27/2009
• Status: Active Grant

• Current Assignee: H2Fuel-Systems B.V.
• Original Assignee: H2Fuel-Systems B.V.
• Inventors: Lugtigheid, Gerardus Wilhelmus
• Primary Examiner(s): LANGEL, WAYNE A
• Application Number:
  US13/146,622
• Publication Number:
  US 20110286913A1
• Time in Patent Office: 1,462 Days
• Field of Search: 366/348, 366/349, 423/648.1, 423/658.2
• US Class Current: 423/648.1
• CPC Class Codes: B67D 7/04 for transferring fuels, lubricants or mixed fuels and lubricants
• CPC Class Codes: C01B 3/065 from a hydride
• CPC Class Codes: Y02E 60/36 Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Abstract

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-) fuelling the hydrogen generating device at a service station and a method for supplying a service station with fuel are provided.

Claims

1. A method for generating hydrogen comprising the steps of:

a) providing a hydrogen carrier fluid comprising hydrogen carrier molecules or particles being dissolved or dispersed in an inert fluid medium;

b) providing an activator fluid comprising water having a conductance value below 0.5 μ

S;

c) injecting the hydrogen carrier fluid and the activator fluid into a first reaction chamber;

wherein

d) the hydrogen carrier fluid and the activator fluid are injected into the reaction chamber in order to cause an intensive mixing of the hydrogen carrier molecules or particles with the activator fluid.

2. The method according to claim 1, wherein the hydrogen carrier fluid and the activator fluid are injected under high pressure.

3. The method according to claim 1, wherein the mixture of the hydrogen carrier fluid and the activator fluid is additionally mixed in a second mixing stage.

4. The method according to claim 3, wherein during the second mixing stage additional activator fluid is added to the mixture of hydrogen carrier fluid and the activator fluid.

5. The method according to claim 3, wherein the additional mixing is effected by a high shear mixer.

6. The method according to claim 3, wherein additional activator fluid is added to the mixture in order to obtain a reaction of the hydrogen carrier fluid and the activator fluid of at least 99%.

7. The method according to claim 1, wherein the generated hydrogen is separated from the reaction residues by a membrane.

8. The method according to claim 1, wherein the total amount of activator fluid is chosen to slightly exceed the stoichiometric amount for the reaction with the amount of hydrogen carrier fluid.

9. The method according to claim 1, wherein the hydrogen carrier is one or more selected from the group consisting of metal hydrides MHx and metal borohydrides M(BH₄)_x, where M is a metal and x denotes the valence of the particular metal.

10. The method according to claim 9, wherein the metal of the hydrogen carrier is selected from the group consisting of Li, Na, Be, Mg, Ca and Al.

11. The method according to claim 10, wherein the hydrogen carrier comprises Ca(BH₄)₂ and/or Al(BH₄)₃.

12. The method according to claim 1, wherein the particle size of the hydrogen carrier particles is 10 microns or smaller.

13. The method according to claim 1, wherein the hydrogen carrier fluid 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.

14. The method according to claim 1, wherein the concentration of the hydrogen carrier molecules in the hydrogen carrier fluid is at least 60%.

15. The method according to claim 1, wherein the viscosity of the hydrogen carrier fluid is from 1 to 2 times that of water at room temperature.

16. The method according to claim 1, wherein the activator is or comprises water and/or an alcohol and/or recycled water from a fuel cell, tap water, or demineralised water.

17. The method according to claim 1, wherein the water is purified, demineralised, treated with reverse osmosis and/or filtered by an electrostatic filter.

18. The method according to claim 1, wherein the activator comprises glycol.

19. The method according to claim 1, wherein an emulsifier is added to the hydrogen carrier fluid or the activator fluid.

20. The method according to claim 1, wherein the method comprises the step of:

providing the reaction chamber with a first heat exchanger, in order to remove a first portion of the heat of the reaction between the hydrogen carrier fuel and activator fluid.

21. The method according to claim 20, wherein the method comprises the step of:

providing the reaction chamber with a second heat exchanger, for removing a second portion of the heat of the reaction between the hydrogen carrier fuel and activator fluid in the mixer.

22. The method according to claim 20, wherein the method comprises the step of providing the heat from the first and or second heat exchanger to a heat conversion cycle which is connected to a steam turbine and drives a generator for generating electrical energy.

23. The method according to claim 20, wherein the method comprises the step of using the heat from the first and or second heat exchanger in a thermo-electric device for direct conversion of heat into electrical energy.

24. The method according to claim 1, wherein the activator fluid is provided through an activator line that is provided with a filter such as to ensure that the conductive value of the water in the activator fluid is below 0.5 μ

S.

25. The method according to claim 1, wherein the hydrogen carrier fluid and the activator fluid are injected inline into the reaction chamber such as to cause the inert fluid medium to be divided into tiny droplets in the activator fluid and to wash away the inert fluid medium from the surface of the hydrogen carrier molecules or particles, in order to cause an intensive mixing and intimate contact of the hydrogen carrier molecules or particles with the activator fluid.

26. The method according to claim 25, wherein the activator fluid is injected as a jet flow.

27. The method according to claim 16, wherein the activator fluid comprises demineralised water treated with reverse osmosis.

28. The method according to claim 27, wherein the demineralised water treated with reverse osmosis is subsequently passed through an electrostatic filter.