Methods and devices for hydrogen generation from solid hydrides

• US 20060269470A1
• Filed: 05/17/2006
• Published: 11/30/2006
• Est. Priority Date: 04/14/2004
• Status: Abandoned Application

• Current Assignee: Millennium Cell Inc.
• Original Assignee: Millennium Cell Inc.
• Inventors: Fennimore, Keith A., Zhang, Qinglin, Eason, Ian, Spallone, John
• Application Number:
  US11/434,766
• Publication Number:
  US 20060269470A1
• Time in Patent Office: Days
• US Class Current: 423/648.100
• CPC Class Codes: B01J 19/2475 Membrane reactors
• CPC Class Codes: B01J 2219/00162 controlling the pressure
• CPC Class Codes: B01J 7/02 by wet methods
• CPC Class Codes: C01B 2203/1604 Starting up the process
• CPC Class Codes: C01B 2203/1609 Shutting down the process
• CPC Class Codes: C01B 3/065 from a hydride
• CPC Class Codes: H01M 8/04216 characterised by the choice for a specific material, e.g. carbon, hydride, absorbent
• CPC Class Codes: Y02E 60/36 Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
• CPC Class Codes: Y02E 60/50 Fuel cells

Abstract

Hydrogen generators and power module systems that use solid chemical hydrides and acidic reagents for hydrogen storage and generation on demand are disclosed. The generators incorporate mechanisms for controlling the contact between solid chemical hydride and acidic reagents to control the rate of hydrogen generation and characteristics of the reaction products, including bulk density. The preferred systems of the present invention combine functions of fuel reagent storage, reaction chamber, and gas-liquid separation into a minimum number of components to reduce the balance of plant of hydrogen generation systems.

Claims

1. An apparatus for hydrogen generation by the acid catalyzed hydrolysis of a solid fuel, comprising:

a solid fuel storage region;

a reaction chamber adapted to contain at least one acidic reagent capable of generating hydrogen upon contact with the solid fuel in the presence of water;

a means for contacting the solid fuel with the acidic reagent in the reaction chamber to produce hydrogen gas and a product;

a hydrogen outlet line in communication with the reaction chamber; and

a hydrogen separator adapted to prevent solids and liquids in the reaction chamber from entering the hydrogen outlet line.

2. The apparatus of claim 1, wherein the means for contacting further comprises a solid fuel dispenser for delivering solid fuel from the storage region to the reaction chamber.

3. The apparatus of claim 2, wherein the solid fuel dispenser comprises a screw feeder, rotary star feeder, or a pellet dispenser.

4. The apparatus of claim 1, wherein the acidic reagent has a water concentration of about 48 M.

5. The apparatus of claim 2, further comprising a controller for controlling the dispensing of the solid fuel from the solid fuel dispenser.

6. The apparatus of claim 5, wherein the controller is configured to use as a control signal at least one of gas pressure in the reaction chamber, temperature of the reaction chamber, the level of materials in the reaction chamber, and power demand of a power module.

7. The apparatus of claim 6 wherein the power module is selected from the group consisting of a fuel cell and a hydrogen-burning engine.

8. The apparatus of claim 6, wherein the power module is selected from the group consisting of a PEM fuel cell, a solid oxide fuel cell, and an alkaline fuel cell.

10. The apparatus of claim 1, further comprising at least one inlet line configured to supply a reagent to the reaction chamber.

11. The apparatus of claim 1, wherein the reaction chamber is permanently attached to the hydrogen generator apparatus.

12. The apparatus of claim 1, wherein the reaction chamber is removably attached to the hydrogen generator apparatus.

13. The apparatus of claim 1, wherein the reaction chamber is configured to store hydrogen.

14. The apparatus of claim 1, wherein the hydrogen separator comprises at least one of a hydrogen permeable membrane or a filter.

15. The apparatus of claim 14, wherein the hydrogen permeable membrane is hydrophobic.

16. The apparatus of claim 14, wherein the hydrogen permeable membrane comprises a material selected from the group consisting of silicon rubber, polyethylene, polypropylene, polyurethane, fluoropolymer, and hydrogen-permeable metal.

17. The apparatus of claim 1, wherein the reaction chamber is partitioned by a moveable wall.

18. The apparatus of claim 17, wherein the reaction chamber further comprises inner and outer walls.

19. The apparatus of claim 18, wherein the inner wall comprises at least one hydrogen separator.

20. The apparatus of claim 19, wherein at least a portion of the at least one hydrogen separator is located in the area traversed by movement of the movable partition.

21. The apparatus of claim 18, wherein the hydrogen outlet is disposed in the outer wall of the reaction chamber.

9. The apparatus of 6 further comprising a conduit configured to transport water generated as a product in the power module from the power module to the reaction chamber.

22. An apparatus for hydrogen generation, comprising:

a storage region adapted to contain an acidic reagent;

a reaction chamber adapted to contain a solid fuel capable of generating hydrogen upon contact with the acidic reagent in the presence of water;

a means for contacting the acidic reagent with the solid fuel in the reaction chamber to produce hydrogen gas and a product;

a hydrogen outlet line in communication with the reaction chamber; and

a hydrogen separator adapted to prevent solids and liquids in the reaction chamber from entering the hydrogen outlet line.

23. The apparatus of claim 22, wherein the reaction chamber is partitioned by a moveable wall.

24. The apparatus of claim 22, wherein the means for contacting comprises a pump for conveying the acidic reagent from the storage region to the reaction chamber.

25. The apparatus of claim 24, wherein the pump is selected from the group consisting of a peristaltic pump, a piezoelectric pump, a piston pump, a diaphragm pump, a centrifugal pump, and an axial flow pump.

26. The apparatus of claim 22, wherein the means for contacting comprises a valve to control the conveyance of the acidic reagent from the storage region to the reaction chamber.

27. The apparatus of claim 26, wherein the valve is selected from the group consisting of a solenoid valve, a ball valve, a pinch valve, and a diaphragm valve.

28. The apparatus of claim 22, wherein the acidic reagent has a water concentration of about 48 M.

29. The apparatus of claim 22, further comprising a controller for controlling the conveying of the acidic reagent from the acidic reagent storage region to the reaction chamber.

30. The apparatus of claim 29, wherein the controller is configured to use as a control signal at least one of gas pressure in the reaction chamber, temperature of the reaction chamber, the level of materials in the reaction chamber, and power demand of a power module.

31. The apparatus of claim 30, wherein the power module is selected from the group consisting of a fuel cell and a hydrogen-burning engine.

32. The apparatus of claim 30, wherein the power module is selected from the group consisting of a PEM fuel cell, a solid oxide fuel cell, and an alkaline fuel cell.

33. The apparatus of claim 22, further comprising at least one inlet line configured to supply a reagent to the reagent storage region.

34. The apparatus of claim 22, further comprising at least one outlet line configured to remove reaction products from the reaction chamber.

35. The apparatus of claim 22, wherein the reaction chamber is permanently attached to the hydrogen generator apparatus.

36. The apparatus of claim 22, wherein the reaction chamber is removably attached to the hydrogen generator apparatus.

37. The apparatus of claim 22, wherein the reaction chamber is configured to store hydrogen.

38. The apparatus of claim 22, wherein the hydrogen separator comprises at least one of a hydrogen permeable membrane or a filter.

39. The apparatus of claim 38, wherein the hydrogen permeable membrane is hydrophobic.

40. The apparatus of claim 38, wherein the hydrogen permeable membrane comprises a material selected from the group consisting of a silicon rubber, polyethylene, polypropylene, polyurethane, fluoropolymer, and a hydrogen-permeable metal.

41. The apparatus of claim 38, wherein the hydrogen-permeable metal membrane comprises a palladium-gold alloy.

42. The apparatus of claim 23, wherein the reaction chamber further comprises inner and outer walls.

43. The apparatus of claim 42, wherein the inner wall comprises at least one hydrogen separator.

44. The apparatus of claim 43, wherein at least a portion of the at least one hydrogen separator is located in the area traversed by movement of the movable partition.

45. The apparatus of claim 42, wherein the hydrogen outlet is disposed in the outer wall of the reaction chamber.

46. A method of generating hydrogen gas by a hydrolysis reaction, comprising:

providing a solid fuel, wherein the solid fuel is capable of generating hydrogen and a product when contacted with an acidic reagent in the presence of water;

providing an acidic reagent; and

contacting the acidic reagent and the solid fuel in a reaction chamber, wherein such contact generates hydrogen gas and a product having a bulk density of at least about 0.7 g/cc.

47. The method of claim 46, wherein the acidic reagent has a water concentration in the range of about 44 M to 52 M.

48. The method of claim 46, wherein the acidic reagent has a water concentration in the range of about 46 M to 50 M.

49. The method of claim 46, wherein the acidic reagent has a water concentration of about 48 M.

50. The method of claim 46, wherein the product is predominately borax pentahydrate.

51. The method of claim 46, wherein the product is predominately boric acid.

52. The method of claim 46, wherein the product is a borate hydrate that is stable to dehydration at temperatures below about 100°

C.

53. The method of claim 46, wherein the product has a bulk density of at least about 1.0 g/cc.

54. The method of claim 46, wherein the product is a solid.

55. The method of claim 46, comprising bringing the solid fuel from a solid fuel storage region into contact with the reagent in a reaction chamber.

56. The method of claim 46, comprising bringing the reagent from a reagent storage region into contact with the solid fuel in a reaction chamber.

57. The method of claim 46, wherein the solid fuel comprises a boron hydride selected from the group consisting of boranes, polyhedral boranes, anions of borohydrides, and anions of polyhedral boranes.

58. The method of claim 46, wherein the solid fuel comprises at least one borohydride salt of formula M(BH₄)_n, wherein M is selected from the group consisting of alkali metal cations, alkaline earth metal cations, aluminum cation, zinc cation, and ammonium cation, and n corresponds to the charge of the selected M cation.

59. The method of claim 58, wherein water and borohydride are provided to the reaction chamber in a molar ratio of about 4:

1 to about 5.3;

1.

60. The method of claim 58, wherein water and borohydride are provided to the reaction chamber in a molar ratio of about 5:

1.

61. The method of claim 46, wherein the acidic reagent and solid fuel are provided to the reaction chamber in about a stoichiometric ratio

62. The method of claim 46, wherein the fuel comprises a material selected from the group consisting of sodium borohydride, lithium borohydride, potassium borohydride, and calcium borohydride, and mixtures thereof.

63. The method of claim 46, wherein the fuel comprises a material selected from the group consisting of sodium borohydride dihydrate, potassium borohydride trihydrate, and potassium borohydride monohydrate, and mixtures thereof.

64. The method of claim 46, wherein the acidic reagent comprises a material selected from the group consisting of hydrochloric acid, sulfuric acid, phosphoric acid, acetic acid, formic acid, maleic acid, citric acid, and tartaric acid.

65. The method of claim 46, wherein the acidic reagent comprises hydrochloric acid.

66. The method of claim 65, wherein the acid has a concentration between 4.4 M and 12 M.

67. The method of claim 46, wherein the acidic reagent comprises sulfuric acid.

68. The method of claim 67, wherein the acid has a concentration between 2.6 M and 7 M.

69. The method of claim 46, further comprising dispensing solid fuel into the reaction chamber through a solid fuel dispensing means.

70. The method of claim 69, wherein the solid fuel dispensing means comprises a screw feeder, rotary star feeder, or a pellet dispenser.

71. The method of claim 46, further comprising supplying reagent through an inlet and removing reaction products through an outlet of the reaction chamber.

72. The method of claim 46, further comprising monitoring at least one of the gas pressure in the reaction chamber, the temperature in the reaction chamber, the level of materials in the reaction chamber, and power demand of a power module.

73. The method of claim 46, wherein the reaction chamber operates at a pressure of about 10 psig to about 200 psig.

74. The method of claim 46, wherein the reaction chamber operates at a pressure of about 50 psig to about 180 psig.

75. The method of claim 46, wherein a partition within the reaction chamber moves to expose at least a portion of a hydrogen separator to reaction products as the partition moves.

76. A method of operating a hydrogen device, comprising:

providing a hydrogen device having a hydrogen gas inlet;

providing a hydrogen generator having a reaction chamber and a hydrogen gas outlet in communication with the inlet of the hydrogen device;

providing a solid fuel capable of generating hydrogen and a product when brought into contact with an acidic reagent and water;

providing an acidic reagent;

contacting the acidic reagent and the solid fuel in the reaction chamber, wherein such contact generates hydrogen gas and a product having a bulk density of at least about 0.7 g/cc; and

separating the hydrogen gas from the product and conveying the gas to the inlet of the hydrogen device through the hydrogen gas outlet.

77. The method of claim 76, wherein the hydrogen device is selected from the group consisting of a fuel cell, a hydrogen-burning engine, and a hydrogen storage device.

78. The method of claim 76, wherein the hydrogen storage device is selected from the group consisting of balloons, gas cylinders, and metal hydrides.

79. The method of claim 76, wherein the hydrogen device is a power module and the reaction chamber stores hydrogen to supply demand of the power module during startup.

80. The method of claim 79, wherein the hydrogen device is a fuel cell selected from the group consisting of a PEM fuel cell, a solid oxide fuel cell, and an alkaline fuel cell.

81. The method of claim 79, further comprising generating electricity in the hydrogen device by oxidizing hydrogen.

82. The method of claim 81, further comprising transporting water generated as a product of generating electricity from the power module to the reaction chamber.

83. The method of claim 82, comprising providing a concentrated acidic reagent and adding water from the power module to the concentrated acidic reagent.

84. The method of claim 76, comprising initially providing a concentrated acidic reagent and subsequently adding water to the concentrated acidic reagent.

85. The method of claim 76, wherein separating the hydrogen comprises use of at least one hydrogen permeable membrane or filter.

86. The method of claim 76, wherein the solid fuel is a borohydride.

87. The method of claim 85, wherein the borohydride is combined with a solid stabilizer selected from the group consisting of metal hydroxides, anhydrous metal metaborates, hydrated metal borates, and mixtures thereof.

88. The method of claim 76, wherein a water soluble co-catalyst is added to the acidic reagent to further catalyze generation of hydrogen from the solid fuel.

89. The method of claim 88, wherein the co-catalyst is selected from the group consisting of the chloride salts of cobalt, nickel, and copper.

90. The method of claim 76, wherein the water concentration of the acidic reagent is about 44 M to about 52 M.

91. The method of claim 76, wherein the water concentration of the acidic reagent is about 46 M to about 50 M.

92. The method of claim 76, wherein the water concentration of the acidic reagent is about 48 M.

93. The method of claim 76, wherein the product is predominately borax pentahydrate.

94. The method of claim 76, wherein the product is predominately boric acid.

95. The method of claim 76, wherein the product has a bulk density of at least about 1.0 g/cc.

96. The method of claim 76, wherein the product is a solid.