1. Field of Invention
This invention relates to a slideable cylindrical valve for controlling the hydrogen flow in fuel cell.
2. Background
Fuel cells, such as PEM fuel cells, use a simple chemical reaction to combine hydrogen and oxygen into water, producing electric current in the process. Hydrogen may be produced by a chemical reaction between a fuel, such as lithium aluminum hydride, and water vapor or by absorption/desorption-adsorption/desorption of hydrogen from a metal hydride. At an anode, hydrogen molecules are ionized by a platinum catalyst, and give up electrons. The proton exchange membrane (PEM) allows protons but not electrons to flow through the membrane. As a result, hydrogen ions flow through the PEM to a cathode, while electrons flow through an external circuit. As the electrons travel through the external circuit, they can perform useful work by powering an electrical device such as an electric motor, light bulb or electronic circuitry. At the cathode, the electrons and hydrogen ions combine with oxygen to form water. The byproducts of the reaction are water and heat.
Valves currently suitable for controlling hydrogen flow in passively regulated micro fuel cells require high tolerances to provide adequate sealing, yet need to be capable of allowing transport of sufficient hydrogen to respond to the demand of the electrical load. High tolerance valves meeting these requirements are difficult to manufacture, expensive, and often require high actuation force.
An electrical power generator includes one or more fuel cells, a fuel chamber enclosing a hydrogen generating fuel, and one or more valves in contact with the fuel chamber. The one or more valves at least partially surrounds the fuel chamber and includes concentric inner and outer components; a fixed component with first perforations, and a slideable component with second perforations and having a plurality of separated flexible sections. In one embodiment, the concentric components are cylindrical and the inner cylindrical component is fixed and the outer cylindrical component is slideable.
A fuel cell system valve includes concentric inner and outer components; a fixed component with first perforations, and a slideable component with second perforations and having a plurality of flexible sections positioned on the slideable cylindrical component. In one embodiment, the concentric components are cylindrical and the inner cylindrical component is fixed and the outer cylindrical component is slideable. The valve at least partially surrounds a hydrogen generating fuel.
In the following description, reference is made to the accompanying drawings that form a part hereof, and in which is shown by way of illustration specific embodiments which may be practiced. These embodiments are described in sufficient detail to enable those skilled in the art to practice the invention, and it is to be understood that other embodiments may be utilized and that structural, logical and electrical changes may be made without departing from the scope of the present invention. The following description of example embodiments is, therefore, not to be taken in a limited sense, and the scope of the present invention is defined by the appended claims.
The electrical power generator described herein generates hydrogen gas internally either through the reaction of water vapor with a chemical hydride fuel or by release of hydrogen from a metal hydride. The hydrogen gas is reacted with atmospheric oxygen from the air at a fuel cell to generate electrical energy. The reaction of hydrogen and oxygen also produces water molecules as a byproduct at the fuel cell. This generated water may be passively diffused from the fuel cell as water vapor to a fuel chamber or cavity that contains the chemical hydride fuel substance, where it reacts with the fuel substance to generate hydrogen gas. The electrical energy generated may be used to power large or small devices that are connected to the power generator, depending on the size of the power generator. The power generator of the embodiments of the invention is particularly useful for powering miniature devices such as wireless sensors, cellular phones or other hand held electronic devices that are electrically connected to the anode and cathode of the one or more fuel cells of the power generator.
Fuel cell stack 125 may include a proton exchange membrane (PEM), catalyst layer, gas diffusion layer, and a micro porous layer. An anode electrode 135 is coupled to the fuel cell stack 125 between the fuel cell stack 125 and the fuel chamber 120. It is also coupled to the anode output electrode 115. A cathode electrode 140 is coupled to the other side of the fuel cell stack, and is coupled to the cathode output electrode 110. It may also be exposed to ambient conditions.
In the embodiments exemplified herein, the electrical power generator and fuel cell system valve are shown having concentric inner and outer cylindrical components; an inner fixed cylindrical component and an outer slideable cylindrical component. It is to be understood that in alternative embodiments, the inner cylindrical component may be slideable and the outer cylindrical component may be fixed.
Between the fuel cell 125 and the hydrogen chamber 120 is a slide valve 143. Slide valve 143 is made up of two cylindrical sleeves that are concentric and adjacent to each other. Slide valve 143 includes a fixed plate 145 and a slideable plate 150 that are coupled in a sliding relationship in one embodiment. A hydrogen and water vapor permeable particulate filter (not shown) may also be used between the fuel cell and the fuel or fuel chamber 120. In one embodiment, the fixed plate 145 is supported in fixed position proximate or adjacent to the fuel chamber 120, and the slideable plate 150 is coupled to a flexible diaphragm 155, that flexes in response to changes in pressure between the hydrogen pressure in the fuel chamber and ambient pressure. A hole 160 provides the diaphragm access to atmospheric pressure. The diaphragm 155 acts as a pressure responsive actuator that controls the slide valve. Each of the fixed plate 145 and slideable plate 150 has openings (such as perforations) that prevent flow when in a closed position and allow flow when the openings (such as perforations) at least partially line up.
The slide valve 143 responds to a pressure differential between ambient and the inside of the power generator. In one embodiment the power generator is cylindrical in shape and the valve plates 145 and 150 are concentric cylinders having mating perforations. Fixed plate 145 and movable plate 150 correspond to an inner cylinder and an outer cylinder respectively. When a pressure differential exists across the membrane 155 such as when hydrogen pressure is greater than ambient pressure, the membrane 155 deflects and moves the outer cylinder 150 axially relative to the inner cylinder. The movement of the outer cylinder relative to the inner cylinder causes the perforations to become misaligned, which closes the valve.
The plates in one embodiment are as thin as possible to maintain high conductance, while maintaining sufficient structural rigidity to move without collapse. Thicker sections on the perimeter of the outer plate running parallel to the direction of movement of the valve may be used to improve structural rigidity while maintaining high conductance. Likewise for the inner plate, where thicker sections may be on the inner diameter.
Other shaped plates may also be used, and may generally conform to the shape of the fuel container and fuel cell. The valve plates may alternatively form a low friction contact fit in one embodiment as illustrated in
Material combinations should have low coefficient of friction facilitate easy sliding. The materials for both the inner and outer plates can be made of the same material, for example stainless steel or brass. Alternatively they can be of different materials, for example stainless steel or brass for the outer valve, and Teflon filled acetal for the inner valve. The inner diameter of the outer plate could be slightly smaller than the outer diameter of the inner plate, creating a sealing force as the outer plate expands to accommodate the inner plate.
In another embodiment, the outer plate could have a cut in the side, with an inside diameter slightly smaller than the outer diameter of the inner plate, such that the outer plate is expanded slightly when placed over the inner plate, and maintains a sealing force against the inner plate.
The lubricant may also operate as a sealant. In one embodiment, the lubricant may be graphite or silicone or other lubricant compatible with materials used and the electrochemical reactions occurring. Oil or other hydrocarbon lubricants may also be used.
Grooves 504 are provided that may contain a flexible material (e.g., a rubber band) wrapped around the circumference of the slideable valve that provide compressive force which holds the moveable valve against the fixed valve, providing a gas seal. When substantially sealed, the transmission of hydrogen through the valve is approximately 1% or less than the fully open transmittance.
The features shown in
In operation, slideable plate 150 may be moved by a diaphragm 155 which is pressure sensitive. If the pressure of matter in the portion of the cell assembly in the volume proximate to slideable plate 150 increases, then diaphragm 155 may bulge out from the chamber volume proximate to slideable plate 150. Attached at about the center of diaphragm 155 may be a linkage 152 that is attached to slideable plate 150. When diaphragm 155 bulges out at the center (upward in the
The valve mechanism described in
The power generator is self regulating based on the pressure and electrical demand. As electrical demand increases, hydrogen is consumed to produce the electricity needed by an electrical load. As the hydrogen is consumed, the pressure in the chamber adjacent to the fuel cells drops, valve 143 opens, and the pressure within the fuel chamber 120 also drops, resulting in the release of more hydrogen. As the electrical demand of the load decreases, less hydrogen is consumed, resulting in an increase in pressure, and preventing the further release of hydrogen from fuel 120. The hydrogen release rate can be very fast, limited only by the rate at which heat can be transferred to the fuel. In this manner, the power generator may provide bursts of power, without great deviation in pressure. The operating temperature may affect the equilibrium pressure within the cell, as the pressure varies with temperature.
The power generator 100 may be maintained at an operating temperature of from about −40° C. to about 85° C., from about −20° C. to about 50° C., from about 0° C. to about 50° C. and from about 20° C. to about 50° C. while in use, for example.
Fuel chamber 120 may contain a chemical hydride, a metal hydride or a mixture thereof.
The chemical hydride is any water-reactive hydrogen-producing material that reacts with water vapor to produce hydrogen. Exemplary chemical hydrides comprise LiAlH4, NaAlH4, KAlH4, MgAlH4, CaH2, LiBH4, NaBH4, LiH, and MgH2, alkali metals, alkaline earth metals, and alkali metal salicides. Specific chemical hydrides comprise LiAlH4, NaAlH4, NaBH4, LiBH4, LiH, or any combination thereof. In one embodiment, the chemical hydride is in the form of pellets.
The chemical hydride pellets may be manufactured with a controlled porosity. The size of the chemical hydride particles that comprise the chemical hydride pellets should be in a range from 1-10 μm diameter to minimize resistance to the flow of water vapor through the chemical hydride, and thus adversely affect the rate of hydrogen generation. The distribution of the chemical hydride particle size can be chosen to optimize for rate of reaction or for hydrogen generation capacity. For example a monodisperse distribution of small chemical hydride particles would allow slow flow of water vapor through the chemical hydride, have a high hydrogen generation capacity but a low rate of hydrogen generation. A monodisperse large particle size distribution would allow faster flow of water vapor through the chemical hydride, have a high rate of hydrogen generation, but have a low hydrogen generation capacity. A bimodal distribution in which smaller particles of chemical hydride fit within the interstices of the larger chemical hydride particles could provide a balance between the rate of hydrogen generation and hydrogen generation capacity. Other particle size distributions are also possible.
Additionally, by varying which chemical hydride is used, the rate of reaction with water vapor can be adjusted, and therefore the rate of hydrogen generation. This can also be accomplished by using mixtures of two or more chemical hydrides. By varying which chemical hydride is used, and at the same time using a mixture of chemical hydrides, and particle size distribution, the rate of reaction of the chemical hydride with water vapor can further be controlled.
The chemical hydride is described herein as a pellet. As used herein this term is used in a broad sense to describe any shape or configuration of the chemical hydride particles that occupy in the space allotted to the chemical hydride in the fuel source. Thus, the shape of the chemical hydride pellet is not critical. It may be a, layer, disk, tablet, sphere, or have no specific shape. The shape of the chemical hydride particles may be determined by the shape of the fuel source and the need to make the most efficient use of the space allotted to the chemical hydride. If appropriate, differently shaped chemical hydride pellets can be used within one fuel source.
The chemical hydride pellet stack may be a part of a removable and disposable or recyclable cartridge for an electrochemical cell such as a fuel cell. In such a cartridge, the metal hydride fuel would be retained in the electrochemical cell, while the stack of chemical hydride pellets and spacers would be removable. Alternatively, the chemical hydride pellets and a portion of the enclosure may be removable from the remainder of the enclosure containing the porous metal hydride. Thus, a fresh chemical hydride pellet stack could replace an exhausted chemical hydride pellet stack allowing the portion of the electrochemical cell containing the porous metal hydride to be reused. For example, the chemical hydride pellet stack can be of a size to fit into an electrical power generator the size of a standard “AA”, “AAA”, “C”, or “D” cell (or any other battery size) that can be removed and replaced. The exhausted chemical hydride pellet stack could also be recycled by addition of new chemical hydride pellets.
Two or more compressed porous chemical hydride pellets may be contacted with, or at least partially surrounded or wrapped, or coated with a flexible, porous water-vapor permeable layer (such as TEFLON, GORE TEX, or NAFION) that prevents fuel particles from expanding into gas diffusion channels adjacent the pellets or other fuel source pellets. The gas diffusion channels may be constructed of porous metal hydride pellets for example. Air gaps may be located between individual chemical hydride pellets, and between the chemical hydride pellets and slide valve 143. A liquid water impermeable, hydrogen and water-vapor permeable membrane or a particulate membrane (such as TEFLON, GORE TEX, or NAFION) may also be positioned between chemical hydride pellets and slide valve 143.
When a chemical hydride is used as fuel, the water formed as a byproduct of an oxygen-hydrogen reaction at the fuel cell 125 may passively diffuse back through the slide valve into the fuel chamber 120. On the anode side 135 of the fuel cell 125, a relatively low humidity region may exist due to a moisture absorbing nature of the fuel substance in fuel chamber 120. Thus, the water retention at the cathode 140 may generate a moisture concentration gradient and a gas pressure differential which causes water molecules to diffuse back through the fuel cell 125 through the slide valve and into fuel chamber 120 in the form of water vapor. This water vapor may react with the chemical hydride fuel in fuel chamber 120 and generate hydrogen gas. The generated hydrogen gas may then pass back through the slide valve and to the fuel cell anode 135 where it can react with oxygen to once again generate electricity and water molecules. This cycle may continue until all of the fuel in chamber 120 is consumed.
In another embodiment, a metal hydride may be chosen as a fuel substance for the fuel storage substance. Metal hydrides function as a sort of hydrogen sponge that can quickly adsorb or desorb hydrogen at an almost constant pressure. Potential metal hydrides include ab5, ab2, ab, complex alloys, intermetallic compounds or solid solution alloys. Specific materials include but are not limited to LaNi5, LaNi4.6Mn0.4, MnNi3.5Cu0.7Al0.8, MnNi4.2Cu0.2Mn0.3Al0.3, TiFe0.8Ni0.2, CaNi5, (V0.9Ti0.1) 0.95Fe0.05, (V0.9Ti0.1) 0.95Fe0.05, and LaNi4.7Al0.3 or any combination thereof.
In one embodiment, an AB5 type materials such as LaNi5, or alloys containing other metals such as aluminum may be used as the reversible metal hydride. The other alloys such as aluminum may be used to tailor the pressure-temperature characteristics of the fuel so that the equilibrium hydrogen pressure at room temperature, approximately 20° C. is in the range of 0.1 PSI up to about 100 PSI or higher. In one embodiment, the pressure ranges up to about 10 PSI to avoid high rates of hydrogen leakage to ambient. Some applications may use even higher pressure with stronger containers. A higher fraction of aluminum results in a lower pressure equilibrium. In one embodiment the metal hydride is such that its equilibrium pressure is in the range of approximately 0.01 to 10 atmospheres over an approximately −20 to 60° C. temperature range.
In one embodiment, the metal hydride fuel storage material is in the form of solid pellets and is approximately 20% porous. The porosity may be varied to control volume expansion and hydrogen generation rate. Multiple pellet segments may be stacked vertically to provide a cylindrical pellet with larger height. The height of the individual segments may also be varied to increase the pellet surface area, which may also increase the hydrogen generation rate.
In one embodiment, fuel chamber 120 includes multiple metal hydride fuel pellets stacked in a vertical relationship. A hydrogen permeable membrane may optionally be disposed about the fuel pellet segments, which may be cylindrical in shape. The membrane may extend over the ends of the stack of fuel pellets in some embodiments. An air gap may be provided between the membrane and fuel pellet if desired.
The metal hydride is described herein as a pellet. As noted above, the term metal hydride pellet used herein this term is used in a broad sense to describe any shape or configuration of the metal hydride that occupies the space allotted to the metal hydride in the fuel source. Thus, the shape in which the porous metal hydride exists is not critical. It may be present as a porous film, web, layer, disk, tablet, sphere, or have no specific shape. The shape of the porous metal hydride pellet may be determined by the shape of the fuel source and the need to make the most efficient use of the space allotted to the metal hydride. If appropriate, differently shaped metal hydride pellets can be used within one fuel source.
In some embodiments, the fuel source comprises a combination of a chemical hydride and a metal hydride. A power generator with a fuel consisting of chemical hydride and metal hydride can accommodate pulses of power by using some of the hydrogen stored in the metal hydride, and can thus be designed for the average power of the range, resulting in lower cost, and reduced self-discharge. Additionally, sensitivity to ambient temperature and humidity may be reduced, because the power generator can draw on the hydrogen stored in the metal hydride.
In one embodiment, two or more chemical hydride pellets may be separated by a metal hydride pellet. The metal hydride may act as both a gas diffusion channel, and as a reversible hydrogen storage element for rapid delivery of hydrogen. The metal hydride may be positioned such that two stacks of chemical hydride pellets are formed. The two or more chemical hydride pellets may be contacted with, or at least partially surrounded or wrapped with a flexible, porous water-vapor permeable layer (such as TEFLON, GORE TEX, or NAFION). Each chemical hydride pellet may be separated by a spacer. Air gaps are between individual chemical hydride pellets, and between the chemical hydride pellets and perforated enclosure. A liquid water impermeable, hydrogen and water-vapor permeable membrane or a particulate membrane (such as TEFLON, GORE TEX, or NAFION) may also be positioned between the pellets and enclosure. A particulate filter may be positioned between the stacks of chemical hydride pellets and slide valve 143.
The walls of fuel chamber 120 may be the same as those of the inner valve or may be a separate structure that is located inside the valve. The enclosure may contain perforations to permit water ingress through the enclosure walls into the outer surface of the pellet, from where water can then diffuse inward. The enclosure may be shaped as a cylinder.
The fuel chamber 120 of the power generator may be sealed and fuel may added through an opening having a removable cover adjacent to or part of the fuel chamber 120 which seals fuel chamber 120 when the cover is in place.
While the present invention has been particularly shown and described with reference to many embodiments, it will be readily appreciated by those of ordinary skill in the art that various changes and modifications may be made without departing from the spirit and scope of the invention. It is intended that the claims be interpreted to cover the disclosed embodiment, those alternatives which have been discussed above and all equivalents thereto.
This application claims the benefit of U.S. Provisional Patent Application 61/223,324 filed Jul. 6, 2009, entitled “FUEL CELL VALVE CONFIGURATION” the contents of which application is incorporated herein by reference in its entirety.
Number | Name | Date | Kind |
---|---|---|---|
2935382 | Osborn et al. | May 1960 | A |
3133837 | Eidensohn | May 1964 | A |
3765946 | Werner et al. | Oct 1973 | A |
3931395 | Beckert et al. | Jan 1976 | A |
3994697 | Burke | Nov 1976 | A |
4048385 | Regnaut | Sep 1977 | A |
4138089 | McCarthy | Feb 1979 | A |
4155712 | Taschek | May 1979 | A |
4261955 | Bailey, Jr. et al. | Apr 1981 | A |
4476196 | Poeppel et al. | Oct 1984 | A |
4476197 | Herceg | Oct 1984 | A |
4596748 | Katz et al. | Jun 1986 | A |
4629664 | Tsukui et al. | Dec 1986 | A |
4659559 | Struthers | Apr 1987 | A |
4826741 | Aldhart et al. | May 1989 | A |
4857420 | Maricle et al. | Aug 1989 | A |
4872472 | Lefevre et al. | Oct 1989 | A |
4876163 | Reichner | Oct 1989 | A |
4906536 | Simonton | Mar 1990 | A |
4910100 | Nakanishi et al. | Mar 1990 | A |
5248125 | Fritch et al. | Sep 1993 | A |
5298341 | Khandkar et al. | Mar 1994 | A |
5372617 | Kerrebrock et al. | Dec 1994 | A |
5443616 | Congdon | Aug 1995 | A |
5449697 | Noaki et al. | Sep 1995 | A |
5534363 | Sprouse et al. | Jul 1996 | A |
5789100 | Burroughs et al. | Aug 1998 | A |
5804329 | Amendola | Sep 1998 | A |
5836750 | Cabuz et al. | Nov 1998 | A |
5849046 | Bailey | Dec 1998 | A |
5851689 | Chen | Dec 1998 | A |
5861221 | Ledjeff et al. | Jan 1999 | A |
5948558 | Amendola | Sep 1999 | A |
5974235 | Nunally et al. | Oct 1999 | A |
5992857 | Ueda et al. | Nov 1999 | A |
6052124 | Stein et al. | Apr 2000 | A |
6054234 | Weiss et al. | Apr 2000 | A |
6093501 | Werth | Jul 2000 | A |
6127058 | Pratt et al. | Oct 2000 | A |
6179986 | Swette et al. | Jan 2001 | B1 |
6250078 | Amendola et al. | Jun 2001 | B1 |
6265093 | Surampudi et al. | Jul 2001 | B1 |
6268076 | Dickmann et al. | Jul 2001 | B1 |
6280869 | Chen | Aug 2001 | B1 |
6303244 | Surampudi et al. | Oct 2001 | B1 |
6307605 | Bailey | Oct 2001 | B1 |
6326097 | Hockaday | Dec 2001 | B1 |
6406808 | Pratt et al. | Jun 2002 | B1 |
6413665 | Blanchet et al. | Jul 2002 | B1 |
6428680 | Kreichauf | Aug 2002 | B1 |
6432566 | Condit et al. | Aug 2002 | B1 |
6433129 | Amendola et al. | Aug 2002 | B1 |
6434278 | Hashimoto | Aug 2002 | B1 |
6468694 | Amendola | Oct 2002 | B1 |
6471850 | Shiepe et al. | Oct 2002 | B2 |
6483275 | Nebrigic et al. | Nov 2002 | B1 |
6497973 | Amendola | Dec 2002 | B1 |
6506510 | Sioui et al. | Jan 2003 | B1 |
6506511 | Lakeman et al. | Jan 2003 | B1 |
6508195 | Tipaldo | Jan 2003 | B1 |
6524450 | Hara | Feb 2003 | B1 |
6524542 | Amendola et al. | Feb 2003 | B2 |
6534033 | Amendola et al. | Mar 2003 | B1 |
6535658 | Mendoza et al. | Mar 2003 | B1 |
6541149 | Maynard et al. | Apr 2003 | B1 |
6544679 | Petillo et al. | Apr 2003 | B1 |
6586563 | Ortega et al. | Jul 2003 | B1 |
6596236 | DiMeo, Jr. et al. | Jul 2003 | B2 |
6610193 | Schmitman | Aug 2003 | B2 |
6620542 | Pan | Sep 2003 | B2 |
6632554 | Doshi et al. | Oct 2003 | B2 |
6638654 | Jankowksi et al. | Oct 2003 | B2 |
6645651 | Hockaday et al. | Nov 2003 | B2 |
6670444 | Amendola et al. | Dec 2003 | B2 |
6672078 | Ovshinsky et al. | Jan 2004 | B2 |
6683025 | Amendola et al. | Jan 2004 | B2 |
6706909 | Snover et al. | Mar 2004 | B1 |
6727012 | Chen et al. | Apr 2004 | B2 |
6728422 | Weiss | Apr 2004 | B1 |
6760488 | Moura et al. | Jul 2004 | B1 |
6801136 | Goodman et al. | Oct 2004 | B1 |
6804949 | Andrews et al. | Oct 2004 | B2 |
6833207 | Joos et al. | Dec 2004 | B2 |
6852436 | Badding et al. | Feb 2005 | B2 |
6866806 | Andrews et al. | Mar 2005 | B2 |
6932847 | Amendola et al. | Aug 2005 | B2 |
6939529 | Strizki et al. | Sep 2005 | B2 |
6942941 | Blunk et al. | Sep 2005 | B2 |
6950030 | Kovarik et al. | Sep 2005 | B2 |
6953009 | Reinke et al. | Oct 2005 | B2 |
6977123 | Burroughs et al. | Dec 2005 | B1 |
7001681 | Wood | Feb 2006 | B2 |
7019105 | Amendola et al. | Mar 2006 | B2 |
7049024 | Leban | May 2006 | B2 |
7073368 | Wood et al. | Jul 2006 | B2 |
7083657 | Mohring et al. | Aug 2006 | B2 |
7105033 | Strizki et al. | Sep 2006 | B2 |
7108777 | Xu et al. | Sep 2006 | B2 |
7128997 | Harding et al. | Oct 2006 | B2 |
7322205 | Bourne et al. | Jan 2008 | B2 |
7367334 | Faison, Jr. et al. | May 2008 | B2 |
7524342 | Brinkley, III | Apr 2009 | B2 |
7527885 | Toukura | May 2009 | B2 |
7691527 | Petillo et al. | Apr 2010 | B2 |
7807131 | Eickhoff | Oct 2010 | B2 |
20010028973 | Ong et al. | Oct 2001 | A1 |
20020068213 | Kaiser et al. | Jun 2002 | A1 |
20020114983 | Frank et al. | Aug 2002 | A1 |
20020154310 | DiMeo, Jr. et al. | Oct 2002 | A1 |
20020177031 | Doshi et al. | Nov 2002 | A1 |
20030009942 | Amendola et al. | Jan 2003 | A1 |
20030044656 | Wood | Mar 2003 | A1 |
20030054215 | Doshi et al. | Mar 2003 | A1 |
20030157018 | Zaluski et al. | Aug 2003 | A1 |
20030235728 | Van Zee et al. | Dec 2003 | A1 |
20040009379 | Amendola et al. | Jan 2004 | A1 |
20040011662 | Xu et al. | Jan 2004 | A1 |
20040033194 | Amendola et al. | Feb 2004 | A1 |
20040035054 | Mohring et al. | Feb 2004 | A1 |
20040047801 | Petillo et al. | Mar 2004 | A1 |
20040053100 | Stanley et al. | Mar 2004 | A1 |
20040101740 | Sanders | May 2004 | A1 |
20040120889 | Shah et al. | Jun 2004 | A1 |
20040148857 | Strizki et al. | Aug 2004 | A1 |
20040161646 | Rezachek et al. | Aug 2004 | A1 |
20040191152 | Amendola et al. | Sep 2004 | A1 |
20040209133 | Hirsch et al. | Oct 2004 | A1 |
20040215407 | Thielman et al. | Oct 2004 | A1 |
20050022883 | Adams et al. | Feb 2005 | A1 |
20050079128 | DeVos et al. | Apr 2005 | A1 |
20050118469 | Leach et al. | Jun 2005 | A1 |
20050132640 | Kelly et al. | Jun 2005 | A1 |
20050135996 | Ortega et al. | Jun 2005 | A1 |
20050136300 | Dyer | Jun 2005 | A1 |
20050142410 | Higashi et al. | Jun 2005 | A1 |
20050158595 | Marsh et al. | Jul 2005 | A1 |
20050166812 | Noll et al. | Aug 2005 | A1 |
20050181245 | Bonne et al. | Aug 2005 | A1 |
20050199546 | Rusta-Sallehy et al. | Sep 2005 | A1 |
20050238573 | Zhang et al. | Oct 2005 | A1 |
20050249993 | Horiuchi et al. | Nov 2005 | A1 |
20050260461 | Wood et al. | Nov 2005 | A1 |
20050262924 | Wood et al. | Dec 2005 | A1 |
20050268555 | Amendola | Dec 2005 | A1 |
20050276746 | Zhang et al. | Dec 2005 | A1 |
20060014059 | Wood | Jan 2006 | A1 |
20060021279 | Mohring et al. | Feb 2006 | A1 |
20060040152 | Wood | Feb 2006 | A1 |
20060045228 | Shiao et al. | Mar 2006 | A1 |
20060102489 | Kelly | May 2006 | A1 |
20060102491 | Kelly et al. | May 2006 | A1 |
20060127722 | Nakajima et al. | Jun 2006 | A1 |
20060144701 | Kelly | Jul 2006 | A1 |
20060174952 | Curello et al. | Aug 2006 | A1 |
20060210850 | Abouatallah et al. | Sep 2006 | A1 |
20060261349 | Doering et al. | Nov 2006 | A1 |
20070026282 | Kumagai et al. | Feb 2007 | A1 |
20070104996 | Eickhoff et al. | May 2007 | A1 |
20070105008 | Gu et al. | May 2007 | A1 |
20070141440 | Yang et al. | Jun 2007 | A1 |
20070190400 | Buche et al. | Aug 2007 | A1 |
20070217994 | Amendola et al. | Sep 2007 | A1 |
20070237995 | Eickhoff et al. | Oct 2007 | A1 |
20070259227 | Oishi et al. | Nov 2007 | A1 |
20070269698 | Gu | Nov 2007 | A1 |
20070271844 | Mohring et al. | Nov 2007 | A1 |
20070275291 | Gu et al. | Nov 2007 | A1 |
20070277870 | Wechsler | Dec 2007 | A1 |
20070287059 | Eickhoff et al. | Dec 2007 | A1 |
20080003484 | Chen et al. | Jan 2008 | A1 |
20080057378 | Kang et al. | Mar 2008 | A1 |
20080090129 | Kunz et al. | Apr 2008 | A1 |
20080107930 | Eickhoff et al. | May 2008 | A1 |
20080124609 | Sasahara et al. | May 2008 | A1 |
20080160383 | Shen et al. | Jul 2008 | A1 |
20080199740 | Giddey et al. | Aug 2008 | A1 |
20080220300 | Jones et al. | Sep 2008 | A1 |
20080241635 | Sato et al. | Oct 2008 | A1 |
20080268299 | Eickhoff et al. | Oct 2008 | A1 |
20080274393 | Markoski et al. | Nov 2008 | A1 |
20080280169 | Niu et al. | Nov 2008 | A1 |
20080280183 | Eun et al. | Nov 2008 | A1 |
20090113795 | Eickhoff | May 2009 | A1 |
20100151283 | Eickhoff | Jun 2010 | A1 |
20100151346 | Eickhoff | Jun 2010 | A1 |
Number | Date | Country |
---|---|---|
19734259 | Feb 1999 | DE |
1351329 | Oct 2003 | EP |
1372205 | Dec 2003 | EP |
1496561 | Jan 2005 | EP |
1372205 | Jul 2005 | EP |
1845572 | Oct 2007 | EP |
1372205 | Oct 2008 | EP |
2055669 | May 2009 | EP |
2056382 | May 2009 | EP |
2055669 | Jan 2010 | EP |
723180 | Feb 1955 | GB |
2164446 | Mar 1986 | GB |
57-138782 | Aug 1982 | JP |
60-000066 | Jan 1985 | JP |
4-342439 | Nov 1992 | JP |
666787 | Mar 1994 | JP |
9-326259 | Dec 1997 | JP |
WO-0035032 | Jun 2000 | WO |
WO-0045457 | Aug 2000 | WO |
WO-0185606 | Nov 2001 | WO |
WO-03084866 | Oct 2003 | WO |
WO-2004025750 | Mar 2004 | WO |
WO-2004035464 | Apr 2004 | WO |
WO-2004075375 | Sep 2004 | WO |
WO-2005004273 | Jan 2005 | WO |
WO-2005013403 | Feb 2005 | WO |
WO-2006113469 | Oct 2006 | WO |
WO-2007134095 | Nov 2007 | WO |
Entry |
---|
“U.S. Appl. No. 11/606,758, Response filed Aug. 17, 2011 to Final Office Action mailed Jun. 24, 2011”, 14 pgs. |
“U.S. Appl. No. 11/606,758, Final Office Action mailed Jun. 24, 2011”, 10 pgs. |
“U.S. Appl. No. 12/335,352 Response filed Nov. 8, 2011 to Restriction Requirement mailed Oct. 12, 2011”, 6 pgs. |
“U.S. Appl. No. 12/335,352, Restriction Requirement mailed Oct. 12, 2011”, 5 pgs. |
“European Application Serial No. 07854813.8, Response filed Jun. 9, 2011 to Office Action mailed Feb. 9, 2011”, 7 pgs. |
“U.S. Appl. No. 12/335,352, Advisory Action mailed Jun. 6, 2012”, 3 pgs. |
“U.S. Appl. No. 12/335,352, Final Office Action mailed Apr. 27, 2012”, 13 pgs. |
“U.S. Appl. No. 12/335,352, Non Final Office Action mailed Dec. 23, 2011”, 10 pgs. |
“U.S. Appl. No. 12/335,352, Preliminary Amendment filed Dec. 15, 2008”, 3 pgs. |
“U.S. Appl. No. 12/335,352, Response filed Jan. 27, 2012 to Non Final Office Action mailed Dec. 23, 2011”, 12 pgs. |
“U.S. Appl. No. 12/335,352, Response filed May 16, 2012 to Final Office Action mailed Apr. 27, 2012”, 14 pgs. |
“U.S. Appl. No. 12/705,423, Preliminary Amendment filed Feb. 10, 2011”, 6 pgs. |
“European Application Serial No. 07854813.8, Office Action mailed Dec. 21, 2011”, 4 pgs. |
“European Application Serial No. 07854813.8, Response filed Apr. 13, 2012 to Office Action mailed Dec. 21, 2012”, 6 pgs. |
“International Application Serial No. PCT/US2007/085766, International Preliminary Report on Patentability dated Jun. 3, 2009”, 6 pgs. |
Aiello, R, et al., “Production of Hydrogen from Chemical hydrides via hydrolysis with steam”, International Journal of Hydrogen Energy, 24, (1999), 1123-1130. |
Amendola, S. C., et al., “A Safe, Portable, Hydrogen Gas Generator Using Aqueous Borohydride Solution and Ru Catalyst”, International Journal of Hydrogen Energy, 25(10), (2000), 969-975. |
Amendola, S. C., et al., “A Novel High Power Density Borohydride-Air Cell”, (Abstract), Electrochemical Society Proceedings; vol. 98-15, (1998), 10 pgs. |
Amendola, S. C., et al., “An Ultrasafe Hydrogen Generator: Aqueous, Alkaline Borohydride Solutins and Ru Catalyst”, (Abstract); Journal of Power Sources, 85(2), (2000), 4 pgs. |
“U.S. Appl. No. 11/592,692, Non-Final Office Action mailed Jul. 23, 2010”, 9 pgs. |
“U.S. Appl. No. 11/592,692, Preliminary Amendment filed Nov. 3, 2006”, 3 pgs. |
“U.S. Appl. No. 11/592,692, Response filed Apr. 28, 2010 to Restriction Requirement mailed Mar. 31, 2010”, 7 pgs. |
“U.S. Appl. No. 11/592,692, Restriction Requirement mailed Mar. 31, 2010”, 6 pgs. |
“U.S. Appl. No. 11/606,758 Final Office Action mailed Sep. 15, 2010”, 9 pgs. |
“U.S. Appl. No. 11/606,758, Examiner Interview Summary Request mailed Mar. 25, 2010”, 1 pg. |
“U.S. Appl. No. 11/606,758, Final Office Action mailed Jun. 10, 2009”, 10 pgs. |
“U.S. Appl. No. 11/606,758, Non-Final Office Action mailed Mar. 25, 2010”, 11 pgs. |
“U.S. Appl. No. 11/606,758, Non-Final Office Action mailed May 12, 2008”, 13 pgs. |
“U.S. Appl. No. 11/606,758, Non-Final Office Action mailed Nov. 13, 2009”, 11 pgs. |
“U.S. Appl. No. 11/606,758, Non-Final Office Action mailed Nov. 24, 2008”, 10 pgs. |
“U.S. Appl. No. 11/606,758, Response filed Feb. 7, 2008 to Restriction Requirement mailed Jan. 7, 2008”, 6 pgs. |
“U.S. Appl. No. 11/606,758, Response filed Feb. 24, 2009 to Non Final Office Action mailed Nov. 24, 2008”, 9 pgs. |
“U.S. Appl. No. 11/606,758, Response filed Jun. 21, 2010 to Non Final Office Action mailed Mar. 25, 2010”, 12 pgs. |
“U.S. Appl. No. 11/606,758, Response filed Jan. 4, 2010 to Non Final Office Action mailed Nov. 13, 2009”, 12 pgs. |
“U.S. Appl. No. 11/606,758, Response filed Nov. 10, 2010 to Final Office Action mailed Sep. 15, 2010”, 13 pgs. |
“U.S. Appl. No. 11/606,758, Response filed Sep. 10, 2009 to Final Office Action mailed Jun. 10, 2009”, 12 pgs. |
“U.S. Appl. No. 11/606,758,, Response filed Aug. 12, 2008 to Non-Final Office Action mailed May 12, 2008”, 11 pgs. |
“U.S. Appl. No. 11/606,759, Restriction Requirement mailed Jan. 7, 2008”, 6 pgs. |
“European Application Serial No. 07854813.8, Office Action mailed Feb. 9, 2011”, 5 pgs. |
“Hobby RC Industry Leaps into the Future with Hydrogen Power”, [online]. http://www.horizonfuelcell.com/files/HorizonpressreleasehcellFeb2010.pdf, Horizon Fuel Cell Technologies, (Feb. 3, 2010), 2 pgs. |
“International Application Serial No. PCT/US2007/085766, International Search Report mailed Apr. 2, 2008”, 4 pgs. |
“International Application Serial No. PCT/US2007/085766, Written Opinion mailed Apr. 2, 2008”, 6 pgs. |
Diaz, H., et al., “Thermodynamic and Structural properties of LaNi5-yAiy compounds and their related hydrides”, International Journal of Hydrogen Energy, 4, (1979), 445-454. |
Melanson, D., “Horizon debuts H-Cell 2,0 hydrogen fuel cell system for R/C cars”, [online]. [retrieved Feb. 18, 2010]. Retrieved from the Internet: <URL: http://www.engadget.com/2010/02/03/horizon-debuts-h-cell-2-0-hydrogen-fuel-cell-system-for-r-c-cars/>, From Engadget Blog, (2010), 3 pgs. |
Mendelsohn, M. H., et al., “The Effect of Aluminum Additions on the Structural and Hydrogen Absorption properties of AB5 Alloys with Particular reference to the LaNi5-xAlx Ternary Alloy System”, Journal of the Less-Common Metals, 63, (1979), 193-207. |
Pasaogullari, U., “Liquid Water Transport in Polymer Electrolyte Fuel Cells with Multi-Layer Diffusion Media”, Proceedings of IMECE04, 2004 ASME International Mechanical Engineering Congress and Exposition, Anaheim, California, (Nov. 13-20, 2004), 1-9. |
“U.S. Appl. No. 12/705,423, Amendment and Response filed Aug. 1, 2012 to Restriction Requirement mailed Jul. 16, 2012”, 5 pgs. |
“U.S. Appl. No. 12/705,383, Non Final Office Action mailed Oct. 3, 2012”, 10 pgs. |
“U.S. Appl. No. 12/705,423, Non Final Office Action mailed Sep. 6, 2012”, 7 pgs. |
“U.S. Appl. No. 12/705,423, Response filed Oct. 16, 2012 to Non Final Office Action mailed Sep. 6, 2012”, 8 pgs. |
“U.S. Appl. No. 12/705,423, Restriction Requirement mailed Jul. 16, 2012”, 5 pgs. |
“U.S. Appl. No. 12/705,383, Response filed Aug. 30, 2012 to Restriction Requirement mailed Aug. 23, 2012”, 7 pgs. |
“U.S. Appl. No. 12/705,383, Restriction Requirement mailed Aug. 23, 2012”, 5 pgs. |
“European Application Serial No. 11153723.9, European Search Report mailed Mar. 22, 2011”, 2 pgs. |
“European Application Serial No. 11153723.9, Office Action mailed May 20, 2011”, 5 pgs. |
“European Application Serial No. 11153723.9, Response filed Sep. 21, 2011 to Office Action mailed May 20, 2011”, 2 pgs. |
“European Application Serial No. 11154088.6, European Search Report mailed May 23, 2011”, 3 pgs. |
“European Application Serial No. 11154088.6, Office Action mailed May 30, 2011”, 5 pgs. |
“European Application Serial No. 11154088.6, Office Action mailed Aug. 22, 2011”, 2 pgs. |
“European Application Serial No. 11154088.6, Response filed Sep. 12, 2011 to Office Action mailed May 30, 2010”, 12 pgs. |
“U.S. Appl. No. 11/606,758, Non Final Office Action mailed May 14, 2013”, 13 pgs. |
“U.S. Appl. No. 12/705,423, Advisory Action mailed May 10, 2013”, 3 pgs. |
Number | Date | Country | |
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20110003237 A1 | Jan 2011 | US |
Number | Date | Country | |
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61223324 | Jul 2009 | US |