IP Library Granted Patent US 7,601,329
Granted Patent B2
US 7,601,329 · App. 10/787,617 · Granted Oct 13, 2009

Regeneration of hydrogen storage system materials and methods including hydrides and hydroxides

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Quick Facts
Patent No.
US 7,601,329
App. No.
10/787,617
Granted
Oct 13, 2009
Kind
B2
Abstract

In one aspect, the invention provides a hydrogen storage composition having a hydrogenated state and a dehydrogenated state. In the hydrogenated state, such composition comprises a hydride and a hydroxide. In a dehydrogenated state, the composition comprises an oxide. The present invention also provides methods of and compositions for regenerating a species of a hydroxide and a hydride material.

Claims (101)

1. A method for releasing hydrogen from hydrogen storage materials comprising:

conducting a hydrogen production reaction by reacting particles of a first hydrogen storage material composition with a substantially chemically equivalent amount of particles of a second hydrogen storage material composition, the reaction being between initially solid particles and for a time and at a temperature sufficient to produce hydrogen (H 2 ) and a solid oxide composition, where said first hydrogen storage material comprises a first hydride and where said second hydrogen storage material comprises a first hydroxide having one or more cationic species other than hydrogen; and

conducting a regeneration reaction utilizing said oxide composition to form a species of a second hydride, a second hydroxide, or both.

2. The method according to claim 1 wherein each of said first and second hydrides has one or more cationic species other than hydrogen and said oxide composition comprises at least one of said one or more cationic species other than hydrogen derived from said first hydride, said first hydroxide, or both.

3. The method according to claim 2 wherein said first hydride and said second hydride are different from one another.

4. The method according to claim 2 wherein said first hydride and said second hydride are the same.

5. The method according to claim 2 wherein said first hydroxide and said second hydroxide are different from one another.

6. The method according to claim 2 wherein said first hydroxide and said second hydroxide are the same.

7. The method according to claim 1 wherein said first hydride is represented by the formula: MI x H x , where MI represents said one or more cationic species other than hydrogen and x represents an average valence state of MI.

8. The method according to claim 1 wherein said first hydroxide is represented by the formula: MII y (OH) y , where MII represents said one or more cationic species other than hydrogen and y represents an average valence state of MII.

9. The method of claim 1 wherein said first hydride is represented by MI x H x and said first hydroxide is represented by MII y (OH) y , where MI and MII respectively represent said one or more cationic species other than hydrogen, and x and y represent average valence states of MI and MII, respectively.

10. The method of claim 9 wherein MI and MII are the same cationic species.

11. The method of claim 9 wherein MI is a complex cationic species comprising two distinct cationic species.

12. The method of claim 9 wherein MII is a complex cationic species comprising two distinct cationic species.

13. The method according to claim 1 wherein said first hydride is selected from the group consisting of: lithium hydride (LiH), lithium borohydride (LiBH 4 ), lithium alanate (LiAlH 4 ), and mixtures thereof.

14. The method according to claim 1 wherein said second hydroxide is lithium hydroxide (LiOH).

15. The method according to claim 1 wherein said first hydride comprises LiH and said first hydroxide comprises LiOH.

16. The method according to claim 15 wherein said hydrogen production reaction proceeds according to a reaction mechanism of LiH+LiOH→Li 2 O+H 2 .

17. The method according to claim 1 wherein said first hydride comprises LiBH 4 and said first hydroxide comprises LiOH.

18. The method according to claim 17 wherein said hydrogen production reaction proceeds according to a reaction mechanism of LiBH 4 +4LiOH→LiBO 2 +2Li 2 O+4H 2 .

19. The method according to claim 1 where said hydride comprises LiBH 4 and said hydroxide comprises LiOH.

20. The method according to claim 19 where said reaction proceeds according to a reaction mechanism of LiBH 4 +4LiOH→LiBO 2 +2Li 2 O+4H 2 .

21. The method according to claim 1 wherein said oxide composition comprises Li 2 O and said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+½H 2 O→LiOH.

22. The method according to claim 1 wherein said regeneration reaction further comprises the following reaction mechanism LiOH+½C→LiH+½CO 2 .

23. The method according to claim 1 wherein said regeneration reaction further comprises the following reaction mechanism LiOH+CO→LiH+CO 2 .

24. The method according to claim 1 wherein said oxide composition comprises Li 2 O and said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+½H 2 +¼C→LiH+¼CO 2 .

25. The method according to claim 1 wherein said oxide composition comprises Li 2 O and said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+¼Si+ 1 / 2 H 2 →LiH+¼SiO 2 .

26. The method according to claim 1 wherein said oxide composition comprises Li 2 O and said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+⅓Cr+ 1 / 2 H 2 →LiH+⅙Cr 2 O 3 .

27. The method according to claim 1 wherein said oxide composition comprises Li 2 O and said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+½Zn+ 1 / 2 H 2 →LiH+½ZnO.

28. The method according to claim 1 wherein said oxide composition comprises Li 2 O and said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+⅓Fe+½H 2 →LiH+⅙Fe 2 O 3 .

29. The method according to claim 1 wherein said oxide composition comprises Li 2 O and said regeneration reaction proceeds according to the reaction mechanism Li 2 O+½N 2 H 4 →LiH+LiOH+½N 2 .

30. A method of producing a source of hydrogen gas comprising: conducting a hydrogen production reaction in a solid hydrogenated starting material composition comprising particles of a starting material hydride and a substantially chemically equivalent amount of particles of a starting material hydroxide, each of said starting material hydride and said starting material hydroxide having one or more cationic species other than hydrogen, to produce hydrogen gas and a solid dehydrogenated reaction product comprising an oxide; and conducting a regeneration reaction by utilizing said dehydrogenated reaction product to form a regenerated hydrogenated material.

31. The method according to claim 30 wherein said regeneration reaction comprises a plurality of reactions to form said regenerated hydrogenated material.

32. The method according to claim 30 wherein said regenerated hydrogenated material is different than said hydrogenated starting material.

33. The method according to claim 30 wherein said regenerated hydrogenated material is the same as said hydrogenated starting material.

34. The method according to claim 30 wherein said regeneration reaction forms said regenerated hydrogenated material comprising a regenerated hydride, a regenerated hydroxide, or both.

35. The method according to claim 34 wherein said starting material hydride and said regenerated hydride are different from one another.

36. The method according to claim 34 wherein said starting material hydride and said regenerated hydride are the same.

37. The method according to claim 34 wherein said starting material hydroxide and said regenerated hydroxide are different from one another.

38. The method according to claim 34 wherein said starting material hydroxide and said regenerated hydroxide are the same.

39. The method according to claim 30 wherein said regeneration reaction comprises said oxide reacting with water to form said regenerated hydrogenated material comprising a regenerated hydroxide.

40. The method according to claim 39 wherein said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+½H 2 O→LiOH.

41. The method according to claim 30 wherein said regeneration reaction comprises reacting a reductant, hydrogen, and a regenerated hydroxide species together to form said regenerated hydrogenated material comprising a regenerated hydride.

42. The method according to claim 30 wherein said regeneration reaction comprises reacting a reductant, hydrogen, and said oxide together to form said regenerated hydrogenated material comprising a regenerated hydride.

43. The method according to claim 42 wherein said reductant possesses more than one oxidation state.

44. The method according to claim 42 wherein said reductant comprises carbon.

45. The method according to claim 42 wherein said reductant is selected from the group consisting of carbon (C), carbon monoxide (CO), magnesium (Mg), aluminum (Al), titanium (Ti), silicon (Si), chromium (Cr), zinc (Zn), iron (Fe), hydrazine (N 2 H 4 ), and mixtures thereof.

46. The method according to claim 42 wherein said reductant is carbon (C).

47. The method according to claim 46 wherein said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+½H 2 +¼C→LiH+¼CO 2 .

48. The method according to claim 46 wherein said regeneration reaction proceeds according to the reaction mechanism LiOH+½C→LiH+½CO 2 .

49. The method according to claim 42 wherein said reductant is carbon monoxide (CO).

50. The method according to claim 49 wherein said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+½H 2 +½CO→LiH+½CO 2 .

51. The method according to claim 49 wherein said regeneration reaction proceeds according to the reaction mechanism LiOH+CO→LiH+CO 2 .

52. The method according to claim 42 wherein said reductant is magnesium (Mg).

53. The method according to claim 52 wherein said regeneration reaction proceeds according to the reaction mechanism Li 2 O+Mg+H 2 →2LiH+MgO.

54. The method according to claim 42 wherein said reductant is aluminum (Al).

55. The method according to claim 54 wherein said regeneration reaction proceeds according to the reaction mechanism 3Li 2 O+2Al+3H 2 →6LiH+Al 2 O 3 .

56. The method according to claim 42 wherein said reductant is titanium (Ti).

57. The method according to claim 56 wherein said regeneration reaction proceeds according to the reaction mechanism Li 2 O+Ti+H 2 →2LiH+TiO.

58. The method according to claim 42 wherein said reductant is silicon (Si).

59. The method according to claim 42 wherein said reductant is chromium (Cr).

60. The method according to claim 42 wherein said reductant is zinc (Zn).

61. The method according to claim 42 wherein said reductant is iron (Fe).

62. The method according to claim 42 wherein said reductant is hydrazine (N 2 H 4 ).

63. The method according to claim 62 wherein said oxide composition comprises Li 2 O and said regeneration reaction proceeds according to the reaction mechanism Li 2 O+½N 2 H 4 →LiH+LiOH+½N 2 .

64. The method according to claim 42 wherein said reductant has a higher oxidation state after said regeneration reaction than prior to said regeneration reaction.

65. The method according to claim 42 wherein said regeneration reaction forms said second hydrogenated material and a secondary byproduct compound comprising said reductant.

66. The method according to claim 65 wherein said secondary byproduct compound comprises a secondary byproduct compound oxide of said reductant.

67. The method according to claim 66 wherein said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+¼Si+½H 2 →LiH+¼SiO 2 .

68. The method according to claim 66 wherein said reductant is silicon (Si) and said secondary byproduct compound oxide is silicon dioxide (SiO 2 ).

69. The method according to claim 66 wherein said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+⅓Cr+½H 2 →LiH+⅙Cr 2 O 3 .

70. The method according to claim 66 wherein said reductant is chromium (Cr) and said secondary byproduct compound oxide is chromium oxide (Cr 2 O 3 ).

71. The method according to claim 66 wherein said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+½Zn+½H 2 →LiH+½ZnO.

72. The method according to claim 66 wherein said reductant is zinc (Zn) and said secondary byproduct compound oxide is zinc oxide (ZnO).

73. The method according to claim 66 wherein said regeneration reaction proceeds according to the reaction mechanism ½Li 2 O+⅓Fe+½H 2 →LiH+⅙Fe 2 O 3 .

74. The method according to claim 66 wherein said reductant is iron (Fe) and said secondary byproduct compound oxide is iron oxide (Fe 2 O 3 ).

75. The method according to claim 66 further comprising providing an additional reductant which reacts with said secondary byproduct compound oxide and thereby reduces the oxidation state of said reductant.

76. The method according to claim 75 wherein said oxidation state of said reduced reductant is equal to an original oxidation state prior to said regeneration reaction.

77. The method according to claim 76 wherein said oxidation state of said reduced reductant is an elemental form of said reductant.

78. The method according to claim 77 wherein said secondary byproduct compound oxide of said reductant is silicon dioxide (SiO 2 ) and said elemental form of said reductant is silicon (Si).

79. The method according to claim 78 wherein said additional reductant is carbon monoxide (CO) which reacts with said silicon dioxide (SiO 2 ) according to the following reaction mechanism ¼SiO 2 +½CO→¼Si+½CO 2 .

80. The method according to claim 77 wherein said secondary byproduct compound oxide of said reductant is chromium oxide (Cr 2 O 3 ), and said elemental form of said reductant is chromium (Cr).

81. The method according to claim 80 wherein said additional reductant is carbon monoxide (CO) which reacts with said chromium oxide (Cr 2 O 3 ) according to the following reaction mechanism ⅙Cr 2 O 3 +½CO→⅓Cr+½CO 2 .

82. The method according to claim 77 wherein said secondary byproduct compound oxide of said reductant is zinc oxide (ZnO), and said elemental form of said reductant is zinc (Zn).

83. The method according to claim 82 wherein said additional reductant is carbon monoxide (CO) which reacts with said zinc oxide (ZnO) according to the following reaction mechanism ½ZnO+½CO→½Zn+½CO 2 .

84. The method according to claim 77 wherein said secondary byproduct compound oxide of said reductant is iron oxide (Fe 2 O 3 ), and said elemental form of said reductant is iron (Fe).

85. The method according to claim 84 wherein said additional reductant is carbon monoxide (CO) which reacts with said iron oxide (Fe 2 O 3 ) according to the following reaction mechanism ½Li 2 O+⅓Fe+½H 2 →LiH+⅙Fe 2 O 3 .

86. The method according to claim 75 wherein said additional reductant comprises carbon (C).

87. The method according to claim 75 wherein said additional reductant comprises carbon monoxide (CO).

88. The method according to claim 30 wherein said starting material hydride is represented by the formula: MI x H x , where MI represents said one or more cationic species other than hydrogen and x represents an average valence state of MI.

89. The method according to claim 30 wherein said starting material hydroxide is represented by the formula: MII y (OH) y , where MII represents said one or more cationic species other than hydrogen and y represents an average valence state of MII.

90. The method of claim 30 wherein said starting material hydride is represented by MI x H x and said starting material hydroxide is represented by MII y (OH) y , where MI and MII respectively represent said one or more cationic species other than hydrogen, and x and y represent average valence states of MI and MII, respectively.

91. The method according to claim 30 wherein said regenerated hydroxide is represented by the formula: MII y (OH) y , where MII represents said one or more cationic species other than hydrogen and y represents an average valence state of MII.

92. The method of claim 30 wherein said regenerated hydride is represented by MI x H x and said regenerated hydroxide is represented by MII y (OH) y , where MI and MII respectively represent said one or more cationic species other than hydrogen, and x and y represent average valence states of MI and MII, respectively.

93. A method for releasing hydrogen from hydrogen storage materials comprising:

conducting an exothermic hydrogen production reaction between particles of a first hydrogen storage material and a substantially chemically equivalent amount of particles of a second hydrogen storage material to produce hydrogen and a byproduct material comprising a solid oxide, where said first hydrogen storage material comprises a hydride composition represented by MI x H x and where said second hydrogen storage material comprises a hydroxide composition represented by MII y (OH) y , where MI and MII represent a cationic species or a mixture of cationic species other than hydrogen, and where x and y represent average valence states of respectively MI and MII; and

conducting a regeneration reaction with said oxide composition to form a species of either a hydride or a hydroxide.

94. The method according to claim 93 wherein said regeneration reaction comprises a plurality of distinct reactions.

95. The method according to claim 93 wherein said regeneration reaction forms both species of a hydride and a hydroxide.

96. The method according to claim 93 wherein at least one of said species of hydride and hydroxide is the same as said hydride composition or said hydroxide composition.

97. The method according to claim 93 wherein both of said species of hydroxide and hydride are the same as said hydride composition and said hydroxide composition.

Assignments (13)
RELEASE OF SECURITY INTEREST Recorded Nov 7, 2014
From: WILMINGTON TRUST COMPANY
To: GM GLOBAL TECHNOLOGY OPERATIONS LLC
Reel/Frame 034371/0676 →
CHANGE OF NAME Recorded Feb 10, 2011
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: GM GLOBAL TECHNOLOGY OPERATIONS LLC
Reel/Frame 025780/0902 →
SECURITY AGREEMENT Recorded Nov 8, 2010
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: WILMINGTON TRUST COMPANY
Reel/Frame 025327/0262 →
RELEASE OF SECURITY INTEREST Recorded Nov 4, 2010
From: UNITED STATES DEPARTMENT OF THE TREASURY
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 025245/0442 →
RELEASE OF SECURITY INTEREST Recorded Nov 4, 2010
From: UAW RETIREE MEDICAL BENEFITS TRUST
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 025311/0770 →
SECURITY AGREEMENT Recorded Aug 28, 2009
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: UAW RETIREE MEDICAL BENEFITS TRUST
Reel/Frame 023162/0001 →
SECURITY AGREEMENT Recorded Aug 27, 2009
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: UNITED STATES DEPARTMENT OF THE TREASURY
Reel/Frame 023156/0052 →
RELEASE OF SECURITY INTEREST Recorded Aug 21, 2009
From: CITICORP USA, INC. AS AGENT FOR BANK PRIORITY SECURED PARTIES; CITICORP USA, INC. AS AGENT FOR HEDGE PRIORITY SECURED PARTIES
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 023127/0468 →
RELEASE OF SECURITY INTEREST Recorded Aug 20, 2009
From: UNITED STATES DEPARTMENT OF THE TREASURY
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 023124/0429 →
SECURITY AGREEMENT Recorded Apr 16, 2009
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: CITICORP USA, INC. AS AGENT FOR BANK PRIORITY SECURED PARTIES; CITICORP USA, INC. AS AGENT FOR HEDGE PRIORITY SECURED PARTIES
Reel/Frame 022553/0446 →
SECURITY AGREEMENT Recorded Feb 4, 2009
From: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
To: UNITED STATES DEPARTMENT OF THE TREASURY
Reel/Frame 022201/0610 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 14, 2009
From: GENERAL MOTORS CORPORATION
To: GM GLOBAL TECHNOLOGY OPERATIONS, INC.
Reel/Frame 022102/0533 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 26, 2004
From: VAJO, JOHN J.; MERTENS, FLORIAN O.; JORGENSEN, SCOTT W.
To: GENERAL MOTORS CORPORATION
Reel/Frame 015032/0655 →