U.S. patent application number 11/516827 was filed with the patent office on 2007-01-11 for proton conducting membrane using a solid acid.
This patent application is currently assigned to California Institute of Technology. Invention is credited to Dane Boysen, Calum Chisholm, Sossina M. Haile, Sekharipuram R. Narayanan.
Application Number | 20070009778 11/516827 |
Document ID | / |
Family ID | 27537464 |
Filed Date | 2007-01-11 |
United States Patent
Application |
20070009778 |
Kind Code |
A1 |
Chisholm; Calum ; et
al. |
January 11, 2007 |
Proton conducting membrane using a solid acid
Abstract
A solid acid material is used as a proton conducting membrane in
an electrochemical device. The solid acid material can be one of a
plurality of different kinds of materials. A binder can be added,
and that binder can be either a nonconducting or a conducting
binder. Nonconducting binders can be, for example, a polymer or a
glass. A conducting binder enables the device to be both proton
conducting and electron conducting.
Inventors: |
Chisholm; Calum; (Pasadena,
CA) ; Narayanan; Sekharipuram R.; (Altadena, CA)
; Boysen; Dane; (Pasadena, CA) ; Haile; Sossina
M.; (Altadena, CA) |
Correspondence
Address: |
TOWNSEND AND TOWNSEND AND CREW, LLP
TWO EMBARCADERO CENTER
EIGHTH FLOOR
SAN FRANCISCO
CA
94111-3834
US
|
Assignee: |
California Institute of
Technology
Pasadena
CA
|
Family ID: |
27537464 |
Appl. No.: |
11/516827 |
Filed: |
September 6, 2006 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
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10139043 |
May 2, 2002 |
7125621 |
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11516827 |
Sep 6, 2006 |
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09439377 |
Nov 15, 1999 |
6468684 |
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10139043 |
May 2, 2002 |
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60151811 |
Aug 30, 1999 |
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60146943 |
Aug 2, 1999 |
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60146946 |
Aug 2, 1999 |
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60116741 |
Jan 22, 1999 |
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Current U.S.
Class: |
429/411 ;
429/442; 429/483; 429/492; 429/516; 429/535 |
Current CPC
Class: |
H01M 6/181 20130101;
B01D 71/00 20130101; C01B 2203/0475 20130101; H01G 9/155 20130101;
Y02P 70/50 20151101; C25B 13/04 20130101; B01D 69/141 20130101;
C01B 2203/047 20130101; H01M 8/0289 20130101; H01M 8/1246 20130101;
B01D 2325/26 20130101; Y02E 60/13 20130101; B01D 53/32 20130101;
H01M 6/18 20130101; H01M 10/0562 20130101; B01D 71/02 20130101;
B01J 19/2475 20130101; H01M 8/1016 20130101; C01B 2203/0405
20130101; B01D 67/0044 20130101; Y02E 60/50 20130101; B01D 67/0055
20130101; C01B 3/501 20130101; H01M 2300/0068 20130101; B01D 53/228
20130101; H01B 1/122 20130101; H01M 8/0631 20130101; B01D 67/0041
20130101; B01D 2257/108 20130101; Y02E 60/10 20130101; H01M 8/0662
20130101 |
Class at
Publication: |
429/033 |
International
Class: |
H01M 8/10 20060101
H01M008/10 |
Goverment Interests
STATEMENT AS TO FEDERALLY SPONSORED RESEARCH
[0002] The invention described herein was made in the performance
of work under a NASA contract and is subject to the provisions of
Public Law 96-517 (U.C.C. 202) in which the Contractor has elected
to retain title.
Claims
1. A proton conducting membrane, formed of a solid acid material in
a solid phase.
2. A membrane as in claim 1 wherein said solid acid material is of
a type that is capable of a superprotonic transition.
3. A membrane as in claim 1 wherein said solid acid material is of
the general form M.sub.aH.sub.b(XO.sub.t).sub.c.
4. A membrane as in claim 3 wherein t is 3 or 4.
5. A membrane as in claim 1 wherein said solid acid material is of
the general form Cs.sub.aH.sub.b(XO.sub.t).sub.c.
6. A membrane as in claim 3 where X is silicon.
7. A membrane as in claim 4 wherein M is Cs.
8. A membrane as in claim 4 wherein M is NH.sub.4.
9. A membrane as in claim 4 wherein said solid acid is of the form
M.sub.aH.sub.b(XO.sub.t).sub.c.nH.sub.2O.
10. A membrane as in claim 4 wherein X is P.
11. A membrane as in claim 3, wherein said solid acid is
CsH.sub.2PO.sub.4.
12. A membrane as in claim 3, wherein said solid acid is
Cs.sub.5(HSO.sub.4).sub.3(H.sub.2PO.sub.4).sub.2.
13. A membrane as in claim 3, wherein said solid acid is
Cs.sub.2(HSO.sub.4).sub.x(H.sub.2PO.sub.4).sub.y.
14. A membrane as in claim 3, wherein said solid acid is
Cs.sub.3(HSO.sub.4).sub.2(H.sub.1.5(S.sub.0.5P.sub.0.5)O.sub.4).
15. A membrane as in claim 3, wherein said solid acid is
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O.
16. A membrane as in claim 3, wherein said solid acid is
TlHSO.sub.4.
17. A membrane as in claim 3, wherein said solid acid is
CsH(SeO.sub.4).sub.x.
18. A membrane as in claim 3, wherein said solid acid is
Cs.sub.2(HSeO.sub.4) (H.sub.2PO.sub.4).
19. A membrane as in claim 3, wherein said solid acid is
(NH.sub.4).sub.3H(SO.sub.4).sub.2.
20. A membrane as in claim 3, wherein said solid acid is
(NH.sub.4).sub.2(HSO.sub.4) (H.sub.2PO.sub.4).
21. A membrane as in claim 3, wherein said solid acid is Rb.sub.3H
(SO.sub.4).sub.2.
22. A membrane as in claim 3, wherein said solid acid is Rb.sub.3H
(SeO.sub.4).sub.2.
23. A membrane as in claim 3, wherein said solid acid is
Cs.sub.1.5Li.sub.1.5H(SO.sub.4).sub.2.
24. A membrane as in claim 3, wherein said solid acid is Cs.sub.2Na
(HSO.sub.4).sub.3.
25. A membrane as in claim 3, wherein said solid acid is
TlH.sub.3(SeO.sub.3).sub.2.
26. A membrane as in claim 3, wherein said solid acid is
CsH.sub.2AsO.sub.4.
27. A membrane as in claim 3, wherein said solid acid is
(NH.sub.4).sub.2(HSO.sub.4) (H.sub.2AsO.sub.4).
28. A membrane as in claim 3, wherein said solid acid is
CaNaHSiO.sub.4.
29. A membrane as in claim 3, further comprising an electrochemical
device, using said membrane for proton transport.
30. A membrane as in claim 1 wherein said solid acid material is
formed of a material that is not water soluble.
31. A proton conducting membrane, formed of an solid acid material
in a superprotonic phase, said solid acid material being of the
general formula M.sub.aH.sub.b(XO.sub.t).sub.c, where t is 3 or 4,
the M material is at least one material from the group consisting
of Li, Be, Na, Mg, K, Ca, Rb, Sr, Cs, Ba, Tl or NH.sub.4.sup.+, and
the X material is at least one material from the group consisting
of Si, P, S, As, Se, or Te.
32. A membrane as in claim 31 wherein said solid acid is non-water
soluble.
33. A method of conducting protons across a barrier, comprising:
forming a membrane from a solid acid material; and using said solid
acid material to conduct protons.
34. A method as in claim 33, wherein said solid acid is of a type
that is capable of a superprotonic transition between a first
temperature and a second temperature; and operating said membrane
as a proton conducting membrane at a temperature between said first
and second temperatures.
35. A method as in claim 33 wherein said solid acid material is of
the general form M.sub.aH.sub.b(XO.sub.t).sub.c.
36. A method as in claim 35 wherein M is Cs.
37. A method as in claim 35 wherein M is NH.sub.4.sup.+.
38. A method as in claim 35 wherein X includes silicon.
39. A method as in claim 33 wherein said protons are conducted in a
fuel cell.
40. A method as in claim 33 wherein said protons are conducted in a
hydrogen separator.
41. A method as in claim 33 wherein said protons are conducted in
an electrolysis cell.
42. A method as in claim 33 wherein said protons are conducted in a
battery.
43. A proton conducting membrane, comprising: an solid acid
material; and a structural binder for said solid acid material,
forming a membrane with said solid acid material.
44. A membrane as in claim 43 wherein said structural binder is a
polymer.
45. A membrane as in claim 44 wherein said solid acid material is a
type capable of a superprotonic transition at a specified
temperature.
46. A membrane as in claim 43 wherein said solid acid material is a
non-water soluble solid acid material.
47. A membrane as in claim 44 wherein said polymer is a melt
processable polymer.
49. A membrane as in claim 44 wherein said polymer is an in-situ
polymerized polymer.
50. A membrane as in claim 43 wherein said structural binder is a
ceramic.
51. A membrane as in claim 43 wherein said structural binder is a
glass.
52. A membrane as in claim 43 wherein said structural binder is
electronically insulating.
53. A membrane as in claim 43 wherein said structural binder is
electrically conducting.
54. A membrane as in claim 53 wherein said conducting material is a
conducting polymer.
55. A membrane as in claim 53 wherein said conducting material is a
metal.
56. A membrane as in claim 55 wherein said metal is mixed with a
polymer.
57. A membrane as in claim 53 wherein said conductor is formed by
direct chemical substitution with variable valence ions.
58. A membrane as in claim 43 wherein said structural binder
includes silicon.
59. A membrane as in claim 43 wherein said structural binder is a
polyester binder.
60. A membrane as in claim 43 wherein said structural binder is
electrochemically unreactive.
61. A membrane as in claim 43 wherein said solid acid is of the of
the general formula M.sub.aH.sub.b(XO.sub.t).sub.c, where: the M
material is a material from the group consisting of Li, Be, Na, Mg,
K, Ca, Rb, Sr, Cs, Ba, Te or NH.sub.4.sup.+, and the X material is
from the group consisting of Si, P, S, As, Se, or Te.
62. A membrane as in claim 61 wherein M is Cs.
63. A membrane as in claim 61 wherein X is Si.
64. A membrane as in claim 61 where M is NH.sub.4.sup.+.
65. A membrane as in claim 61 wherein said solid acid material is a
solid acid material.
66. A membrane as in claim 61 wherein said solid acid material is
water insoluble.
67. A membrane as in claim 53 wherein said solid acid material is
processed to include variable valence elements.
68. A fuel cell as in claim 67, wherein said solid-acid material is
water insoluble.
69. A fuel cell as in claim 67, wherein said solid acid material is
of the general formula M.sub.aH.sub.b(XO.sub.t).sub.c, where: the M
group is a material from the group consisting of Li, Be, Na, Mg, K,
Ca, Rb, Sr, Cs, Ba, Tl or NH.sub.4.sup.+, and the X material is
from the group consisting of Si, P, S, As, Se, or Te.
70. A method of operating an electrochemical device comprising:
providing a fuel to a proton conducting membrane; and carrying out
an electrochemical reaction at said proton conducting membrane,
without humidifying said membrane.
71. A method as in claim 70, wherein said carrying out comprises
operating at a temperature of 100.degree. degrees C. or higher.
72. A method as in claim 70, wherein said proton conducting
membrane includes an solid acid material.
73. A method as in claim 70, wherein said proton conducting
membrane includes an solid acid material in a superprotonic
phase.
74. A method as in claim 72, wherein said proton conducting
membrane includes a binder.
75. A method as in claim 74, wherein said solid acid material is of
the general formula M.sub.aH.sub.b(XO.sub.4).sub.c, where: the M
group is a material from the group consisting of Li, Be, Na, Mg, K,
Ca, Rb, Sr, Cs, Ba, Tl or NH.sub.4.sup.+, and the X material is
from the group consisting of Si, P, S, As, Se, or Te.
76. A proton and electron conducting membrane, formed of an solid
acid material.
77. A membrane as in claim 76 wherein said solid acid material is
of a type that is capable of a superprotonic transition at a
specified temperature.
78. A membrane as in claim 76 wherein said solid acid material is
of the general formula M.sub.aH.sub.b(XO.sub.t).sub.c.
79. A membrane as in claim 76 wherein said solid acid material is a
solid acid material.
80. A membrane as in claim 78 where X includes silicon.
81. A membrane as in claim 76, further comprising a binder for the
solid acid material.
82. A membrane as in claim 76 wherein said binder includes a
conducting material.
83. A membrane as in claim 82 wherein said conducting material
includes a conductive polymer.
84. A membrane as in claim 82 wherein said conducting material
includes a metal material.
85. A membrane as in claim 76 wherein said solid acid material has
free valence electrons.
86. A method of separating H.sub.2 from other materials,
comprising: chemically reacting a H.sub.2 at a surface of a proton
and electron conducting membrane which is formed of materials
including a solid acid material, to decompose said H into H+ and
e-; and using said membrane formed of an solid acid material to
allow said H+ and e- to pass while blocking other materials
including CO from passing.
87. A proton conducting membrane comprising; a Cs based solid acid
material; and a melt processable polymer binder for said solid acid
material, forming a membrane with said solid acid material.
88. A membrane as in claim 87 wherein said Cs based solid acid is
one of
CS.sub.3(HSO.sub.4).sub.2(H.sub.1.5(S.sub.0.5P.sub.0.5)O.sub.4),
Cs.sub.3(HSO.sub.4).sub.2(H.sub.2PO.sub.4),
Cs.sub.5(HSO.sub.4).sub.3(H.sub.2PO.sub.4).sub.2 or
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4)CsHSO.sub.4, CsHSeO.sub.4 or
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O.
89. A membrane as in claim 87 wherein said melt processable polymer
is polyvinylidine fluoride.
90. A membrane as in claim 87 wherein said membrane is formed by
hot pressing.
91. A proton conducting membrane, comprising: a NH.sub.4 based
solid acid material; and a structural binder for said solid acid
material, forming a membrane with said solid acid material.
92. A membrane as in claim 91 wherein said structural binder is a
melt processable polymer.
93. A membrane as in claim 91 wherein said solid acid is one of
CsH.sub.2PO.sub.4,
Cs.sub.5(HSO.sub.4).sub.3(H.sub.2PO.sub.4).sub.2,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.3(HSO.sub.4).sub.2(H.sub.2PO.sub.4).sub.2,
Cs.sub.3(HSO.sub.4).sub.2(H.sub.1.5(S.sub.0.5P.sub.0.5)O.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O, TlHSO.sub.4,
CsHSeO.sub.4, CS.sub.2(HSeO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.3H(SeO.sub.4).sub.2(NH.sub.4).sub.3H(SO.sub.4).sub.2,
(NH.sub.4).sub.2(HSO.sub.4)(H.sub.2PO.sub.4), Rb.sub.3H
(SO.sub.4).sub.2, Rb.sub.3H(SeO.sub.4).sub.2,
Cs.sub.1.5Li.sub.1.5H(SO.sub.4).sub.2, Cs.sub.2Na(HSO.sub.4).sub.3,
TlH.sub.3(SeO.sub.3).sub.2,
CsH.sub.2AsO.sub.4(NH.sub.4).sub.2(HSO.sub.4)(H.sub.2AsO.sub.4),
T.sub.eO.sub.4, or CaNaHSiO.sub.4.
94. A proton conducting membrane, comprising: a solid acid silicate
of the general form M.sub.AH.sub.BSiO.sub.4 used in a proton
conducting membrane.
95. A membrane as in claim 94 further comprising a structural
binder for said solid acid material.
96. A membrane as in claim 94 wherein said solid acid is one of
CaNaHSiO.sub.4, Cs.sub.3HSiO.sub.4 or
(NH.sub.4).sub.3HSiO.sub.4.
97. A proton conducting membrane, comprising: a Cs or NH.sub.4
based solid acid; and a ceramic or glass binder, forming a
structural binder for said solid acid.
98. A device as in claim 97 wherein said binder is porous.
99. A method of using an electrochemical device, comprising:
forming a solid acid material into a proton conducting membrane;
and using said solid acid membrane to conduct protons.
100. A method as in claim 99 further comprising heating said solid
solid acid material to a temperature at which it undergoes a
superprotonic transition, prior to said using.
101. A method as in claim 99 wherein said solid solid acid compound
is a sulfate or sulfate phosphate type solid acid.
102. A method as in claim 99 wherein said solid solid acid compound
is a selenate or selenate phosphate solid acid.
103. A method as in claim 99 wherein said solid solid acid is a
silicate.
104. A method as in claim 99 wherein said forming comprises adding
a binder to said material.
105. A method as in claim 104 wherein said binder is a polymer.
106. A method as in claim 104 wherein said binder is a
ceramic/oxide glass.
107. A material as in claim 104 wherein said binder is a conducting
metal or semiconductor.
108. A method of operating an electrochemical device, comprising:
forming a membrane using a solid acid material of the general form
M.sub.aH.sub.b(XO.sub.t).sub.c; and using said solid solid acid
material to conduct protons in the electrochemical device.
109. A membrane as in claim 31, wherein said solid acid is a solid
solid acid material.
110. A proton conducting membrane, formed of a solid acid material
in a superprotonic phase.
111. A method of operating an electrochemical device comprising:
providing a fuel to a proton conducting membrane which includes a
carbon monoxide material therein, and carrying out an
electrochemical reaction at said proton conducting membrane,
without removing said carbon monoxide material.
112. A method of forming a membrane-electrode assembly, comprising:
forming a composite film including a polymer and an solid acid of
the general form M.sub.aH.sub.b(XO.sub.t).sub.c; forming said
composite film onto a backing; forming electrodes on said backing;
and hot pressing said material to form an assembly.
113. A method as in claim 112, wherein an solid acid to polymer
volume ratio is 50/50.
114. A method as in claim 112, wherein said backing is graphite
paper.
115. A method as in claim 33, wherein said protons are conducted in
a supercapacitor.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] This application is a divisional application of and claims
priority to U.S. application Ser. No. 09/439,377, filed Nov. 15,
1999, which claims the benefit of U.S. provisional applications
Ser. No. 60/116,741, filed Jan. 22, 1999, Ser. No. 60/146,946,
filed Aug. 2, 1999, Ser. No. 60/146,943 filed Aug. 2, 1999, and
Ser. No. 60/151,811, filed Aug. 30, 1999.
FIELD
[0003] The present application describes a proton conducting
membrane formed using an solid acid in its solid phase. More
specifically, the present application teaches a proton conducting
membrane, formed using an solid acid mixed with a supporting binder
material, that is impermeable to fluids such as gas and is water,
can operate without hydration, and has high proton Ha
conductivity.
BACKGROUND
[0004] Proton conducting materials have a number of applications.
Proton conducting membranes are widely utilized in devices which
use a chemical reaction to produce or store electricity, or use
electricity to drive a chemical process. Materials which conduct
both protons and electrons ("mixed proton and electron conductors")
are utilized in related applications.
[0005] Electrochemical devices depend on the flow of protons, or
the flow of both protons and electrons through a proton conducting
membrane. Exemplary electrochemical devices include a fuel cell, an
electrolysis cell, a hydrogen separation cell, a battery, a
supercapacitor, and a membrane reactor. There are other
electrochemical devices which also use a proton conducting
membrane.
[0006] An important use for proton conducting membranes is in fuel
cells. Fuel cells are attractive alternatives to combustion engines
for the generation of electricity because of their higher
efficiency and the lower level of pollutants they produce. A fuel
cell generates electricity from the electrochemical reaction of a
fuel e.g. methane, methanol, gasoline, or hydrogen, with oxygen
normally obtained from air.
[0007] There are three common types of fuel cells used at
temperatures close to ambient. A direct hydrogen/air fuel cell
system stores hydrogen and then delivers it to the fuel cell as
needed.
[0008] In an indirect hydrogen/air fuel cell, hydrogen is generated
on site from a hydrocarbon fuel, cleaned it of carbon monoxide
(CO), and subsequently fed to the fuel cell.
[0009] A direct methanol fuel cell ("DMFC"), feeds methanol/water
solution directly to the fuel cell, e.g., without any fuel
processing. One type of DMFC has been described, for example, in
U.S. Pat. No. 5,559,638. There are various advantages and
disadvantages inherent within all three configurations. All are, to
a greater or lesser extent, limited by the performance of the
proton conducting membrane.
[0010] Nafion.TM., a perfluorinated sulphonic acid polymer, is
often used as a membrane material for fuel cells which operate at
temperatures close to ambient. Other hydrated polymers have also
been used as proton conductive materials. Membranes of modified
perfluorinated sulfonic acid polymers, polyhydrocarbon sulfonic
acid polymers, and composites thereof are also known. These and
related polymers are used in hydrated form. Proton transport occurs
by the motion of hydronium ions, H.sub.3O.sup.+. Water is necessary
in order to facilitate proton conduction. Loss of water immediately
results in degradation of the conductivity. Moreover, this
degradation is irreversible--a simple reintroduction of water to
the system does not restore the conductivity. Thus, the electrolyte
membranes of these hydrated polymer-based fuel cells must be kept
humidified during operation. This introduces a host of
balance-of-plant needs for water recirculation and temperature
control.
[0011] A second limitation derives from the need to maintain water
in the membrane. In order to maintain hydration, the temperature of
operation cannot exceed 100.degree. C. without cell pressurization.
High temperature operation could be desirable, however, to increase
catalyst efficiency in generating protons at the anode (in both
H.sub.2 and direct methanol fuel cells) and to improve catalyst
tolerance to carbon monoxide ("CO"). CO is often present in the
fuel that is used in the fuel cells. The CO can poison the precious
metal catalysts. This is particularly problematic in indirect
hydrogen/air fuel cells for which hydrogen is generated on site.
High temperatures also benefit the reduction reaction on the
cathode.
[0012] Another limitation of hydrated polymer electrolytes occurs
in applications in methanol fuel cells. These polymers can be
permeable to methanol. Direct transport of the fuel (i.e. methanol)
across the membrane to the air cathode results in losses in
efficiency.
[0013] Alternate proton conducting materials, which do not require
humidification, which can be operated at slightly elevated
temperatures, and/or which are impermeable to methanol, are
desirable for fuel cell applications.
[0014] In the field of hydrogen separation, a proton conducting
membrane is utilized to separate hydrogen from other gases such as
CO and/or CO.sub.2. Palladium is often used for this application.
Palladium is permeable to molecular hydrogen, but not in general to
other gases. There are drawbacks to the use of this material. It is
expensive and the hydrogen diffusion rate is low. It would be
desirable to develop new materials which are less expensive and
exhibit higher proton/hydrogen transport rates.
[0015] In general, materials utilized in other electrochemical
devices such as electrolysis cells, batteries, supercapacitors,
etc., include liquid acid electrolytes, which are highly corrosive,
and solid polymer proton conductors, which require humidification
or exhibit insufficient proton conductivity. High conductivity,
high chemical and thermal stability solid membranes with good
mechanical properties are desirable for all of these
applications.
SUMMARY
[0016] The present specification defines a new kind of material for
a proton conducting membrane. Specifically, a proton conducting
material is formed using an solid acid. The solid acid can be of
the general form M.sub.aH.sub.b(XO.sub.t).sub.c or
M.sub.aH.sub.b(XO.sub.t).sub.c.nH.sub.2O,
where:
[0017] M is one or more of the species in the group consisting of
Li, Be, Na, Mg, K, Ca, Rb, Sr, Cs, Ba, Tl and NH.sub.4.sup.+ or
Cu.sup.+;
[0018] X is one or more of the species in the group consisting of
Si, P, S, As, Se, Te, Cr and Mn; and
[0019] a, b, c, n and t are rational numbers.
[0020] Solid acids do not rely on the presence of hydronium ions
for proton transport, thus they do not require hydration for use as
proton conductors.
[0021] A preferred solid acid used according to this specification
is a solid phase solid acid that exhibits a superprotonic phase, a
phase in which the solid has disorder in its crystal structure and
a very high proton conductivity.
[0022] An embodiment uses a structural binder or matrix material to
enhance the mechanical integrity and/or chemical stability of the
membrane. That structural binder can be many different kinds of
materials in the different embodiments. In particular, the
structural binder can be a polymer, a ceramic, or an oxide
glass.
[0023] Another embodiment uses an electronically conducting
material as a matrix. This creates a membrane which conducts both
protons and electrons.
[0024] The resulting material can be used for a proton conducting
material in a device that relies on the flow of protons or the flow
of both protons and electrons across a membrane, herein an
"electrochemical" device e.g. a fuel cell, a hydrogen separation
membrane, or a electrolysis cell.
BRIEF DESCRIPTION OF THE DRAWINGS
[0025] FIG. 1 shows an exemplary hydrogen/air fuel cell using an
solid acid supported by a binder as its proton conducting
membrane.
[0026] FIG. 2 shows an exemplary direct methanol fuel cell using an
solid acid supported by a binder as its proton conducting
membrane
[0027] FIG. 3 shows a hydrogen separation membrane for the removal
of CO and other gases from hydrogen;
[0028] FIG. 4 shows another type of hydrogen separation membrane
made of a proton conducting composite; and
[0029] FIGS. 5 and 6 show a membrane reactor.
DETAILED DESCRIPTION
[0030] The present application teaches using an solid acid as a
proton conducting membrane.
[0031] A solid acid can be of the general form
M.sub.aH.sub.b(XO.sub.t).sub.c.nH.sub.2O,
[0032] where:
[0033] M is one or more of the species in the group consisting of
Li, Be, Na, Mg, K, Ca, Rb, Sr, Cs, Ba, Ti and NH.sub.4.sup.+;
[0034] X is one or more of the species in the group consisting of
Si, P, S, As, Se, Te, Cr and Mn; and
[0035] a, b, c, n and t are rational numbers; with t preferably
being 3 or 4, and where t.gtoreq.0.
[0036] The solid acids used herein are compounds, such as
CsHSO.sub.4, whose properties are intermediate between those of a
normal acid, such as H.sub.2SO.sub.4, and a normal salt, such as
Cs.sub.2SO.sub.4. In general, the chemical formula of the solid
acids of the type used according to the present specification can
be written as a combination of the salt and the acid.
[0037] In general, solid acids are comprised of oxyanions, for
example SO.sub.4, SO.sub.3 SeO.sub.4, SeO.sub.3, SiO.sub.4,
PO.sub.4 or AsO.sub.4, etc., which are linked together via O--H . .
. O hydrogen bonds. The structure may contain more than one type of
XO.sub.4 or XO.sub.3 group, and may also contain more than one type
of M species.
[0038] Certain solid acids are solid materials at room
temperature.
[0039] Many different solid acids are contemplated by this
specification. One example of a material that can be used as the
solid acid is CsHSO.sub.4, which is intermediate between
Cs.sub.2SO.sub.4 (a normal salt) and H.sub.2SO.sub.4 (a normal
acid). In this case, the solid acid can be written as 0.5
Cs.sub.2SO.sub.4*0.5 H.sub.2SO.sub.4. Another example, using the
same salt and the same acid, is 1.5 Cs.sub.2SO.sub.4*0.5
H.sub.2SO.sub.4, to give Cs.sub.3H(SO.sub.4).sub.2.
[0040] Other examples are:
[0041] CsH.sub.2PO.sub.4,
Cs.sub.5(HSO.sub.4).sub.3(H.sub.2PO.sub.4).sub.2,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.3(HSO.sub.4).sub.2(H.sub.2PO.sub.4),
Cs.sub.3(HSO.sub.4).sub.2(H.sub.1.5(S.sub.0.5P.sub.0.5)O.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O, TlHSO.sub.4,
CsHSeO.sub.4, Cs.sub.2(HSeO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.3H(SeO.sub.4).sub.2(NH.sub.4).sub.3H(SO.sub.4).sub.2,
(NH.sub.4).sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Rb.sub.3H(SO.sub.4).sub.2, Rb.sub.3H(SeO.sub.4).sub.2,
Cs.sub.1.5Li.sub.1.5H(SO.sub.4).sub.2, Cs.sub.2Na(HSO.sub.4).sub.3,
TlH.sub.3(SeO.sub.3).sub.2,
CsH.sub.2AsO.sub.4(NH.sub.4).sub.2(HSO.sub.4)(H.sub.2AsO.sub.4),
CaNaHSiO.sub.4
[0042] The preferred material for any specific electrochemical
device depends on the application. For example,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4) may be preferred for
electrochemical devices where high conductivity is critical.
(NH.sub.4).sub.3H(SO.sub.4).sub.2 may be preferred where low cost
is critical. CaNaHSiO.sub.4 may be preferred where chemical
stability is critical.
[0043] Solid acids have certain characteristics that can be
advantageous when used as a proton conducting membrane. The proton
transport process does not rely on the motion of hydronium ions,
thus solid acids need not be humidified and their conductivity is
substantially independent of humidity. Another advantage is that
solid acids are generally stable against thermal decomposition at
elevated temperatures. The thermal decomposition temperature for
some of the solid acids described in this specification, e.g.,
CaNaHSiO.sub.4, can be as high as 350.degree. C. Since solid acids
need not be humidified, solid acid based membranes can be operated
at elevated temperatures, e.g. temperatures above 100.degree.
C.
[0044] The conductivity of solid acids may be made purely protonic,
or both electronic and protonic depending on the choice of the X
element in the chemical formula
M.sub.aH.sub.b(XO.sub.4).sub.c.nH.sub.2O or
M.sub.aH.sub.b(XO.sub.3).sub.c.nH.sub.2O. That is, by using a given
amount of a variable valence element such as Cr or Mn for X, the
solid acid can be made to conduct electrons as well as protons.
[0045] Another advantage is caused by the structure of the solid
acids themselves. Since solid acids are dense, inorganic materials,
they are impermeable to gases and other fluids that may be present
in the electrochemical environment, e.g., gases and hydrocarbon
liquids.
[0046] The materials are also relatively inexpensive.
[0047] This combination of properties: good conductivity in dry
environments, conductivity which can be controlled to be either
purely proton conducting or both electron and-proton conducting,
impermeability to gases and hydrocarbon liquids, serviceability at
elevated temperatures, e.g. temperatures over 100.degree. C. and
relatively low cost, render solid acids as useful materials for use
as membranes in electrochemical devices.
[0048] Solid acids exhibit another advantageous property for
applications in proton conducting membranes. Under certain
conditions of temperature and pressure, the crystal structure of a
solid acid can become disordered. Concomitant with this disorder is
an high conductivity, as high as 10.sup.-3 to 10.sup.-2
.OMEGA..sup.-1cm.sup.-1. Because of the high proton conductivity of
the structurally disordered state, it is known as a superprotonic
phase. The proton transport is believed to be facilitated by rapid
XO.sub.4 or am XO.sub.3 group reorientations, which occur because
of the disorder.
[0049] Many solid acids enter a superprotonic state at a
temperature between 50 and 150.degree. C. at ambient pressures. The
transition into the superprotonic phase may be either sharp or
gradual. The superprotonic phase is marked by an increase in
conductivity, often by several orders of magnitude. At temperatures
above the transition temperature, the solid acid is superprotonic
and retains its high proton conductivity until the decomposition or
melting temperature is reached.
[0050] Solid acids that undergo a superprotonic transition
include:
[0051] CsHSO.sub.4, Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.3(HSO.sub.4).sub.2(H.sub.2PO.sub.4),
Cs.sub.3(HSO.sub.4).sub.2(H.sub.1.5(S.sub.0.5P.sub.0.5)O.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O, CsHSeO.sub.4,
Cs.sub.3H(SeO.sub.4).sub.2, (NH.sub.4).sub.3H(SO.sub.4).sub.2,
Rb.sub.3H(SeO.sub.4).sub.2.
[0052] The superprotonic phases of solid acids have increased
conductivity. An interesting embodiment is a solid acid operated at
a temperature above the superprotonic transition temperature, and
below the decomposition or melt temperature.
[0053] Despite the many advantageous properties of solid acids,
problems can be encountered in trying to implement them in
electrochemical devices because many solid acids are water soluble.
They can also be difficult to process into large area membranes,
and they often have poor mechanical properties. Some solid acids,
such as CaNaHSiO.sub.4 and other silicates, are not soluble in
water.
[0054] Because of these difficulties, a disclosed embodiment
includes a composite comprised of an solid acid embedded in a
supporting matrix. The solid acid part of the composite provides
the desired electrochemical activity, whereas the matrix provides
mechanical support and also may increase chemical stability.
Different materials are contemplated herein for use as the
supporting matrix.
[0055] In light of the properties of solid acids outlined above,
the preferred embodiment is a composite material comprised of a
solid acid embedded in a supporting matrix and operated at a
slightly elevated temperature. In such a composite, the solid acid
is in its superprotonic phase, exhibits high conductivity, and
provides the desired electrochemical functions; the support matrix
may provide mechanical support, and it may also serve to protect
the solid acid from water in the environment. A high temperature of
operation can render the solid acid into its superprotonic state. A
high temperature of operation can also ensure that any water
present in the electrochemical device will be present in the form
of steam rather than liquid water, making the H.sub.2O less likely
to attack the solid acid.
[0056] Hydrogen/Air Fuel Cells
[0057] A hydrogen/air fuel cell is shown in FIG. 1, in which the
proton conducting membrane is a solid acid/matrix composite of the
type described herein. Because the membrane need not be humidified,
the fuel cell system can be simpler than one which uses a hydrated
polymer membrane. The humidification system normally required for
fuel cell utilizing a Nafion or related polymer membrane can be
eliminated in FIG. 1. Hence, less rigid temperature monitoring and
control may be used in the solid acid based system as compared with
Nafion based fuel cell systems. These differences allow a
less-costly fuel cell system.
[0058] Because the membrane need not be humidified, the fuel cell
shown in FIG. 1 can be operated at temperatures above 100.degree.
C. The tolerance of the Pt/Ru catalysts to carbon monoxide CO
poisoning increases with increasing temperature. Thus, a fuel cell
such as shown in FIG. 1, operated at a temperature above
100.degree. C. may withstand higher concentrations of CO in the
hydrogen fuel than a Nafion based fuel cell which is typically
operated at a temperature lower than 100.degree. C.
[0059] The high temperature of operation also enhances the kinetics
of the electrochemical reactions, and can thereby result in a fuel
cell with higher overall efficiency than one based on Nafion or
other hydrated polymers.
[0060] Direct Methanol Fuel Cells
[0061] A direct methanol fuel cell is shown in FIG. 2. The proton
conducting membrane is a solid acid/matrix composite of the type
described herein. Because the membrane need not be humidified, the
fuel cell system is much simpler and thus less costly than state of
the art direct methanol fuel cell systems. The humidification
system.normally required for fuel cell utilizing a Nafion or
related polymer membrane is eliminated in FIG. 2. Furthermore,
temperature monitoring and control in the solid acid based system
does not need to be as tight as in Nafion based fuel cell systems.
Because the solid acid based membrane need not be humidified, the
fuel cell may be operated at elevated temperatures. High
temperatures can enhance the kinetics of the electrochemical
reactions. This can result in a fuel cell with very high
efficiency.
[0062] Another significant advantage of the fuel cell shown in FIG.
2 over state of the art direct methanol fuel cells results from the
decreased permeability of the membrane to methanol. In state of the
art direct methanol fuel cells, in which Nafion or another hydrated
polymer serves as the membrane, methanol cross-over through the
polymeric membrane lowers fuel cell efficiencies. The
impermeability of a solid acid membrane can improve this
efficiency.
[0063] Hydrogen Separation Membranes
[0064] The Ru/Pt catalyst in a hydrogen/air fuel cell is sensitive
to CO poisoning, particularly at temperatures close to ambient.
Therefore, in an indirect hydrogen/air fuel cell, the hydrogen
produced by the reformer is often cleaned, of e.g. CO to below 50
ppm, before it enters the fuel cell for electrochemical
reaction.
[0065] In FIG. 3, a hydrogen separation membrane is shown for the
removal of CO and other gases from hydrogen. The hydrogen
separation membrane is made of a mixed proton and electron
conducting membrane, as described herein. Hydrogen gas, mixed with
other undesirable gases, is introduced onto one side of the
membrane. Clean hydrogen gas is extracted from the other side of
the membrane.
[0066] On the inlet side of the membrane, hydrogen gas is
dissociated into H+ and e-. Because the membrane is both proton
conducting and electron conducting, both of these species can
migrate through the membrane. However, the membrane is if
substantially impermeable to other gases and fluids. Hence, CO and
other undesirable gases or fluids cannot so migrate. On the outlet
side of the membrane, the H+ and e- recombine to form hydrogen gas.
The overall process is driven by the hydrogen chemical potential
gradient, which is high on the inlet side of the membrane and low
on the outlet side of the membrane.
[0067] Another type of hydrogen separation membrane is shown in
FIG. 4. The membrane is made of a proton conducting composite of
the type described herein, and is connected to a current source.
Hydrogen gas, mixed with other undesirable gases, is introduced
onto one side of the membrane and clean hydrogen gas is extracted
from the other side of the membrane. Application of a current
causes the hydrogen gas to dissociate into H+ and e- . Because the
membrane conducts only protons, these protons are the only species
which can migrate through the membrane. The electrons migrate
through the current source to the outlet side of the membrane,
where the H+ and e- recombine to form hydrogen gas. The membrane is
substantially impervious to other gases and fluids. Hence, CO and
other undesirable gases or fluids cannot migrate through the proton
conducting membrane. The overall process is driven by electric
current applied via the current source.
[0068] Membrane Reactors
[0069] In FIG. 5 a membrane reactor is shown, in which a mixed
proton and electron conducting membrane of the type described
herein is utilized. The general reaction is that reactants A+B
react to form products C+D, where D is hydrogen gas. Use of a mixed
proton and electron conducting membrane in this reactor can enhance
the reaction to give yields that exceed thermodynamic equilibrium
values. On the inlet side of the membrane reactor, the reactants
form products C+H2. Under equilibrium conditions, the hydrogen
concentration builds up and the forward reaction is slowed. With
the use of the mixed hydrogen and electron conducting membrane, the
hydrogen is immediately extracted from the reaction region via
transport through the membrane, and the forward reaction is
enhanced. Examples of reactions in which yield could be enhanced by
using such a membrane reactor include (1) the steam reformation of
methane (natural gas) to produce syngas: CH4+H2O.fwdarw.CO+3H2; (2)
the steam reformation of CO to produce CO2 and H2:
CO+H2O.fwdarw.CO2+H2; (3) the decomposition of H2S to H2 and S, (4)
the decomposition of NH3 to H2 and N2; (4) the dehydrogenation of
propane to polypropylene; and (5) the dehydrogenation of alkanes
and aromatic compounds to various products.
[0070] In FIG. 6 a second type of membrane reaction is shown,
again, utilizing a mixed proton and electron conducting membrane of
the type described herein. In this case, the general reaction is
that the reactants A+B form the products C+D, where B is hydrogen.
The hydrogen enters the reaction region via transport through the
mixed conducting membrane, whereas the reactant A is introduced at
the inlet to the membrane reactor, and is mixed with other species.
The manner in which the hydrogen is introduced into the reactant
stream (through the membrane) ensures that only the reactant A, and
none of the other species reacts with hydrogen. This effect is
termed selective hydrogenation.
[0071] The mixed proton and electron conducting membranes described
herein provide an advantage over state-of-the-art membranes in that
the conductivity is high at temperatures as low as 100.degree. C.,
and the membranes are relatively inexpensive. Selective
hydrogenation at temperatures close to ambient may have particular
application in synthesis of pharmaceutically important compounds
which cannot withstand high temperatures.
[0072] According to a first class of materials, the solid acid is
mixed with a supporting structure that is electrochemically
unreactive, to form a composite. A first embodiment uses a solid
acid mixed with a melt-processable polymer as the supporting matrix
structure.
[0073] The solid acid (CHS) was prepared from aqueous solutions
containing stoichiometric amounts of Cs.sub.2CO.sub.3 and
H.sub.2SO.sub.4. Crystalline CsHSO.sub.4 and a small amount
(.about.8 wt %) of the related compound
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O (which also exhibits
superprotonic behavior) were obtained upon introduction of methanol
into the solution. Composite membranes of the solid acid and
poly(vinylidene fluoride) were prepared by simple melt-processing
methods. The two components were lightly ground together then
hot-pressed at 180.degree. C. and 10 kpsi for 15 minutes. Volume
ratios of CHS:PVDF from 100% CsHSO.sub.4 to 100% PVDF were prepared
in 10 vol % increments.
[0074] Another example of a composite contains a solid acid and a
thermoset polymer, which can be mixed in with the solid acid in
monomer or prepolymer form, and then polymerized in situ.
[0075] The solid acid (CHS) was prepared from aqueous solutions
containing stoichiometric amounts of Cs.sub.2CO.sub.3 and
H.sub.2SO.sub.4. Crystalline CsHSO.sub.4 and a small amount
(.about.8 wt %) of the related compound
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O (which also exhibits
superprotonic behavior) were obtained upon introduction of methanol
into the solution. Composite membranes of the solid acid and the
polyester resin marketed under the name Castoglas by Buehler, Inc.
were synthesized simply by lightly grinding the solid acid and
pre-polymer together and then adding the
polymerization/crosslinking catalyst. A material with a 50:50
volume ratio was prepared.
[0076] Another example of a thermoset polymer--solid acid composite
comprises the solid acid (NH.sub.3).sub.3H(SO.sub.4).sub.2 and the
polymer poly(dicyclopentadiene) or poly DCPD.
[0077] The solid acid, TAHS, was prepared from aqueous solutions of
(NH.sub.4).sub.2SO.sub.4 and H.sub.2SO.sub.4. The solid acid was
ground then mixed with the monomer dicyclopentadiene. The
polymerization catalyst was introduced into the mixture, which was
then poured onto a Teflon plate and pressed into a thin film. The
film was cured at 100.degree. C. for approximately 2 hours.
Materials with 25 and 17 vol % TAHS were prepared.
[0078] Another method for preparing solid acid/polymer composites
is suspension coasting. For this, CsHSO.sub.4 was dissolved in a
water/ethanol solution. The polymer PVDF was then dispersed into
this solution. A composite membrane was formed by casting the
suspension and allowing the solvents to evaporate. Composite
membranes comprised of a solid acid and a non-polymeric matrix
material, such as a ceramic or an oxide glass can be prepared in
the following manner. The solid acid is synthesized form aqueous
solution and the matrix material is synthesized separately. The two
components are mixed and ground together. The mixture is then hot
pressed, preferably at a temperature which causes the solid acid to
melt and flow, to yield a dense composite membrane.
[0079] The nature of the chemical bonding in solid acids of general
formula M.sub.aH.sub.b(XO.sub.4).sub.c.nH.sub.2O or
M.sub.aH.sub.b(XO.sub.3).sub.c.nH.sub.2O where:
[0080] M is one or more of the species in the group consisting of
Li, Be, Na, Mg, K, Ca, Rb, Sr, Cs, Ba, Tl and NH.sub.4.sup.+;
[0081] X is one or more of the species in the group consisting of
Si, P, S, As, Se, and Te; and
[0082] a, b, c, and n are rational numbers, and n can be zero.
[0083] leads to materials which are inherently poor conductors of
electrons. These compounds can be used in devices which require
both proton and electron transport directly through the membrane if
a mechanism for electron transport is introduced.
[0084] The first approach for introducing electronic conductivity
into solid acid based materials is to prepare a composite comprised
of the solid acid and a second substance which has a high
electronic conductivity. This second substance may be an
electronically conducting polymer, such as poly(aniline), or a
typical metal, such as aluminum or copper. Where the electronically
conducting component is a metal, it may be advantageous to
introduce a chemically and electrically inert polymer into the
composite simply to serve as a binder and provide the membrane with
good mechanical properties. The processing methods described above
may be used to prepare such composite membranes.
[0085] The second approach for introducing electronic conductivity
into solid acid based materials is to perform direct chemical
substitutions with variable valence ions. For example, a portion of
the sulfur in CsHSO.sub.4 may be replaced by chromium, which can be
present in an oxidation state of anywhere from 2+ to 6+. Similarly,
manganese may be introduced on the sulfur site, as this ion
exhibits valence states anywhere between 2+ and 7+. Chemical
substitution may also be performed with respect to the cesium in a
compound such as CsHSO.sub.4. Large ions with variable valence,
such as thallium, indium, lead and tin can be used for these
substitutions. The solid acid so modified may be used in an
electrochemical device directly, or may be combined with a
supporting matrix material as described above.
[0086] In the FIG. 1 embodiment, a membrane-electrode assembly
(MEA) is prepared from the CHS--PVDF composite film in which the
solid acid to polymer volume ratio is 50:50. The electrodes are
formed of graphite paper which is impregnated with a complex slurry
of platinum powder, PVDF, the solid acid, and Nafion,
suspended/dissolved in a water and isopropanol solution. After
evaporation of the solvents, the electrodes so prepared are
hot-pressed onto the composite membrane. The MEA is placed in a
fuel cell test station at 140.degree. C. and hydrogen is introduced
at the anode and oxygen at the cathode. The open cell voltage (OCV)
obtained in this manner was 0.88 V. The same type of MEA may also
be used in the FIG. 2 embodiment.
VII. EXAMPLES
Example 1
[0087] A Cs based solid acid such as CsHSO.sub.4, CsHSeO.sub.4 or
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O is ground and mixed with
a melt-processable polymer binder, such as poly(vinylidene
fluoride), and hot-pressed. The result forms a solid composite
membrane which is proton conducting even in dry atmospheres. The
composite membrane, being comprised of two components whicha re
substantially impermeable to fluids, may be less permeable than
Nafion.TM..
Example 2
[0088] A Cs based solid acid such as
Cs.sub.3(HSO.sub.4).sub.2(H.sub.1.5(S.sub.0.5P.sub.0.5)O.sub.4),
Cs.sub.3(HSO.sub.4).sub.2(H.sub.2P.sub.4),
Cs.sub.5(HSO.sub.4).sub.3(H.sub.2PO.sub.4).sub.2 or
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4) is ground and mixed with a
melt-processable polymer binder, such as poly(vinylidene fluoride),
and hot-pressed. The result forms a solid composite membrane which
is proton conducting even in dry atmospheres. The membrane is also
less permeable to fluids than Nafion.TM..
Example 3
[0089] A NH.sub.4 based solid acid such as (NH.sub.4).sub.3H
(SO.sub.4).sub.2 or (NH.sub.4).sub.3H(SeO.sub.4).sub.2 is ground
and mixed with a melt-processable polymer binder, such as Crystar
101 thermoplastic, and hot-pressed. The result forms a solid
composite membrane which is proton conducting even in dry
atmospheres. The membrane is less permeable to fluids than
Nafion.TM. and is also less expensive.
Example 4
[0090] An solid acid silicate of general formula
M.sub.aH.sub.bSiO.sub.4, such as CaNaHSiO.sub.4,
Cs.sub.3HSiO.sub.4, (NH.sub.4).sub.3HSiO.sub.4, is used as a
membrane. Some of these materials are water insoluble and may have
sufficient structural integrity that a binder is not required in
some applications.
Example 5
[0091] A Cs or NH.sub.4 based solid acid, such as CsHSO.sub.4,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O or
(NH.sub.4).sub.3H(SO.sub.4).sub.2 is mixed with the prepolymer of a
resin such as "castoglas", a commercial product from Buehler, Inc.
The polymerization/crosslinking catalyst is added to the mixture,
and a solid composite membrane so formed. The in situ
polymerization/crosslinking can lead to a higher impermeability
than composites formed by melt-processing.
Example 6
[0092] A Cs or NH.sub.4 based solid acid, such as CsHSO.sub.4,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O or
(NH.sub.4).sub.3H(SO.sub.4).sub.2 is mixed with a monomer such as
dicyclopentadiene. A polymerization catalyst is then added to the
mixture, and a solid composite membrane comprised of the solid acid
and poly(dicyclopentadiene) is formed. The in situ polymerization
of the polymer can lead to a higher impermeability than composites
formed by melt-processing. Use of a NH.sub.4 based solid acid can
result in an inexpensive membrane.
Example 7
[0093] A Cs or NH.sub.4 based solid acid, such as CsHSO.sub.4,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4xH.sub.2O or
(NH.sub.4).sub.3H(SO.sub.4).sub.2 is dissolved in water, and added
to a suspension of an insoluble polymer such as poly(vinylidene
fluoride) suspended in a fluid such as ethanol. The mixture is cast
and the liquids (water and ethanol) allowed to evaporate. This
procedure yields a composite membrane which is proton conducting
even in dry atmospheres. The casting step can produce very thin
membranes, with thicknesses on the order of one hundred
microns.
Example 8
[0094] A Cs or NH.sub.4 based solid acid, such as CsHSO.sub.4,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH2O or (NH.sub.4).sub.3H
(SO.sub.4).sub.2 is ground and mixed with a ceramic, such as
Al.sub.2O.sub.3, or an oxide glass, such as amorphous SiO.sub.2.
The mixed powders are compressed by hot-pressing. The resulting
composite membrane may be stable to higher temperatures than those
in which the binder is a polymer.
Example 9
[0095] A Cs or NH.sub.4 based solid acid, such as CsHSO.sub.4,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O or
(NH.sub.4).sub.3H(SO.sub.4).sub.2 is dissolved in water. The
solution is introduced into a porous membrane comprised of an inert
binder such as Teflon.TM., SiO.sub.2, or Al.sub.2O.sub.3. The water
is allowed to evaporate, leaving the solid acid to fill the pores
of the binder. The result is a composite membrane which is proton
conducting even in dry atmospheres.
Example 10
[0096] A Cs or NH.sub.4 based solid acid, such as CsHSO.sub.4,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O or
(NH.sub.4).sub.3H(SO.sub.4).sub.2, which is only proton conducting,
is ground and mixed with an electronically conducting polymer such
as poly(anylene). The composite membrane formed can conduct both
protons and electrons.
Example 11
[0097] An solid acid silicate of general formula
M.sub.aH.sub.bSiO.sub.4, such as CaNaHSiO.sub.4, Cs.sub.3HSiO.sub.4
or (NH.sub.4).sub.3HSiO.sub.4, is ground and mixed with an
electronically conducting polymer such as poly(anilene). The
composite membrane formed can conduct both protons and
electrons.
Example 12
[0098] A proton conducting solid acid, such as CsHSO.sub.4,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
(NH.sub.4).sub.3H(SO.sub.4).sub.2 or CaNaHSiO.sub.4, and a metal,
such as Ag, Au, or Cu, are ground and mixed. The mixed powders are
compressed by hot-pressing. The composite membrane formed can
conduct both protons and electrons, and may be stable to higher
temperatures than a composite in which the electron conducting
component is a polymer.
Example 13
[0099] A proton conducting solid acid, such as CsHSO.sub.4,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
(NH.sub.4).sub.3H(SO.sub.4).sub.2 or CaNaHSiO.sub.4, and a metal,
such as Ag, Au, or Cu, are ground and mixed. A polymeric material
is also added. A solid composite membrane is prepared either by
hot-pressing, if the polymer is melt-processable such as
poly(vinylidene fluoride), or by in situ polymerization, if the
polymer is in situ polymerizable such as poly(dicyclopentadiene).
The composite membrane is both proton and electron conducting, and
may have superior mechanical properties to a composite containing
only a solid acid and a metal.
Example 14
[0100] A mixed electron and proton conducting solid acid, such as
CsHCr.sub.xS.sub.1-xO.sub.4 or
(NH.sub.4).sub.3H(Cr.sub.xS.sub.1-xO.sub.4).sub.2 in which one of
the X elements has a variable valence, is mixed with an inert
polymeric binder. If the polymer is melt-processable, such as
poly(vinylidene fluoride), a membrane is formed by hot-pressing. If
the polymer can be polymerized in situ, a membrane is formed by
mixing the solid acid, the monomer and the polymerization catalyst.
The resulting membrane conducts both protons and electrons, and may
be more stable in oxidizing atmospheres than a composite containing
metal particles.
Example 15
[0101] A Cs or NH.sub.4 based solid acid, such as CsHSO.sub.4,
Cs.sub.2(HSO.sub.4)(H.sub.2PO.sub.4),
Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O or
(NH.sub.4).sub.3H(SO.sub.4).sub.2 is prepared from aqueous
solution, ground, and then pressed into a thin membrane. The
membrane is used in an electrochemical device at a temperature
above the superprotonic transition temperature and above
100.degree. C., so that the proton conductivity of the solid acid
is high and any H.sub.2O that may be present in the device exists
in the form of steam rather than liquid water.
Example 16
[0102] A mixed electron and proton conducting solid acid, such as
CsHCr.sub.xS.sub.1-xO.sub.4 or (NH.sub.4).sub.3H
(Cr.sub.xS.sub.1-xO.sub.4).sub.2 in which one of the X elements has
a variable valence, is prepared from aqueous solution or by solid
state reaction. The powder is then ground and pressed into a thin
membrane. The membrane is used in an electrochemical device at a
temperature above the superprotonic transition temperature and
above 100.degree. C., so that the conductivity of the solid acid is
high and any H.sub.2O that may be present in the device exists in
the form of steam rather than liquid water.
Example 17
[0103] A composite comprised of one or more of the solid acids
listed in Table 1 and one or more of inert binders listed in Table
2. If one or more of the components in the composite is
electronically conducting, the composite membrane will be capable
of conducting both protons and electrons. Electronically conducting
substances are indicated. TABLE-US-00001 TABLE 1 Solid acid
compounds. Sulfates and selenates and sulfate-phosphates selenate
phosphates silicates CsHSO.sub.4 CsHSeO.sub.4 CaNaHSiO.sub.4
Cs.sub.3H(SO.sub.4).sub.2 Cs.sub.3H(SeO.sub.4).sub.2
CaH.sub.2SiO.sub.4 Cs.sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O
Cs.sub.5H.sub.3(SeO.sub.4).sub.4.xH.sub.2O CsH.sub.3SiO.sub.4
Cs.sub.3(HSO.sub.4).sub.2(H.sub.1.5(S.sub.0.5P.sub.0.5)O.sub.4)
Cs.sub.3(HSeO.sub.4).sub.2(H.sub.1.5(Se.sub.0.5P.sub.0.5)O.sub.4)
Cs.sub.2H.sub.2SiO.sub.4 Cs.sub.3(HSO.sub.4).sub.2(H.sub.2PO.sub.4)
Cs.sub.3(HSeO.sub.4).sub.2(H.sub.2PO.sub.4) Cs.sub.3HSiO.sub.4
Cs.sub.2(HSO.sub.4) (H.sub.2PO.sub.4) Cs.sub.2(HSeO.sub.4)
(H.sub.2PO.sub.4) NH.sub.4H.sub.3SiO.sub.4
Cs.sub.5(HSO.sub.4).sub.3(H.sub.2PO.sub.4).sub.2
Cs.sub.5(HSeO.sub.4).sub.3(H.sub.2PO.sub.4).sub.2
(NH.sub.4).sub.2H.sub.2SiO.sub.4 CsH.sub.2PO.sub.4
(NH.sub.4).sub.3HSiO.sub.4 NH.sub.4HSO.sub.4 NH.sub.4HSeO.sub.4
RbH.sub.3SiO.sub.4 (NH.sub.4).sub.3H(SO.sub.4).sub.2
(NH.sub.4).sub.3H(SeO.sub.4).sub.2 Rb.sub.2H.sub.2SiO.sub.4
(NH.sub.4).sub.5H.sub.3(SO.sub.4).sub.4.xH.sub.2O
(NH.sub.4).sub.5H.sub.3(SeO.sub.4).sub.4.xH.sub.2O
Rb.sub.3HSiO.sub.4 (NH.sub.4).sub.2(HSO.sub.4) (H.sub.2PO.sub.4)
(NH.sub.4).sub.2(HSeO.sub.4) (H.sub.2PO.sub.4) KH.sub.3SiO.sub.4
(NH.sub.4)H.sub.2PO.sub.4 K.sub.2H.sub.2SiO.sub.4 RbHSO.sub.4
RbHSeO.sub.4 K.sub.3HSiO.sub.4 Rb.sub.3H(SO.sub.4).sub.2
Rb.sub.3H(SeO.sub.4).sub.2 NaH.sub.3SiO.sub.4
Rb.sub.5H.sub.3(SO.sub.4).xH.sub.2O
Rb.sub.5H.sub.3(SeO.sub.4).sub.4.xH.sub.2O Na.sub.2H.sub.2SiO.sub.4
Rb.sub.2(HSO.sub.4) (H.sub.2PO.sub.4) Rb.sub.2(HSeO.sub.4)
(H.sub.2PO.sub.4) Na.sub.3HSiO.sub.4 RbH.sub.2PO.sub.4
BaCsHSiO.sub.4
[0104] TABLE-US-00002 TABLE 2 Binder or matrix materials
ceramic/oxide metal or Polymer glass semiconductor poly(vinylidene
fluoride) SiO.sub.2 Ag* poly(dicyclopentadiene) Al.sub.2O.sub.3 Au*
poly(tetraflouroethelyne) MgO Cu* [Teflon] poly(ether-ether ketone)
cordierite Al* po1y (ether sulfone) Ni* Silicones [dimethyl Fe*
siloxane polymers] poly(pyrrole)* Zn* poly(aniline)* graphite*
silicon* *electronically conducting
[0105] Other modifications are within the disclosed embodiment. For
example, the above has described the materials having a
superprotonic transition upon heating. Certain materials may have
their superprotonic transition temperature below room temperature.
Thus, there may be no apparent superprotonic transition and the
material would be disordered at room temperature. These solid acids
with structural disorder even prior to heating are also
contemplated.
* * * * *