|Publication number||US20020127141 A1|
|Application number||US 09/788,768|
|Publication date||Sep 12, 2002|
|Filing date||Feb 20, 2001|
|Priority date||Feb 20, 2001|
|Also published as||US6460733|
|Publication number||09788768, 788768, US 2002/0127141 A1, US 2002/127141 A1, US 20020127141 A1, US 20020127141A1, US 2002127141 A1, US 2002127141A1, US-A1-20020127141, US-A1-2002127141, US2002/0127141A1, US2002/127141A1, US20020127141 A1, US20020127141A1, US2002127141 A1, US2002127141A1|
|Original Assignee||Acker William P.|
|Export Citation||BiBTeX, EndNote, RefMan|
|Referenced by (49), Classifications (10), Legal Events (7)|
|External Links: USPTO, USPTO Assignment, Espacenet|
 1. Field of the Invention
 The present invention relates generally to the field of fuel cells and, more specifically, to a fuel container and delivery system for a liquid feed direct oxidation fuel cell.
 2. Background Information
 Fuel cells are devices in which an electrochemical reaction is used to generate electricity. A variety of materials may be suited for use as a fuel depending upon the materials chosen for the components of the cell. Organic materials, such as methanol or formaldehyde, are attractive choices for fuel due to the their high specific energy.
 Fuel systems may be divided into “reformer-based” (i.e., those in which the fuel is processed in some fashion before it is introduced into the cell) or “direct oxidation” in which the fuel is fed directly into the cell without internal processing. Most currently available fuel cells are of the reformer-based type, but field-processing requirements for such cells limits the applicability of those cells to relatively large systems.
 Direct oxidation fuel cell systems may be better suited for a number of applications such as smaller mobile devices (i.e., mobile phones, handheld and laptop computers), as well as in larger applications. One example of a direct oxidation system is the direct methanol fuel cell system or DMFC. In a DMFC, the electrochemical reaction at the anode is a conversion of methanol and water to C0 2, H+ and e−. More specifically, a liquid hydrocarbon solution (typically aqueous methanol) is applied to a protonically-conductive (but, electrically non-conductive) membrane directly using a catalyst on the membrane surface to enable direct oxidation of the hydrocarbon on the anode. The hydrogen protons are separated from the electrons and the protons pass through the membrane electrolyte, which is impermeable to the electrons. The electrons thus seek a different path to reunite with the protons and travel through a load, providing electrical power.
 The carbon dioxide, which is essentially a waste product, is separated from the remaining methanol fuel before such fuel is re-circulated. In an alternative usage of the carbon dioxide this gas can be used to passively pump liquid methanol into the feed fuel cell. This is disclosed in U.S. patent application Ser. No. 09/717,754, filed on Dec. 8, 2000, for a PASSIVELY PUMPED LIQUID FEED FUEL CELL SYSTEM, which is commonly owned by the assignee of the present invention, and which is incorporated by reference herein in its entirety .
 The methanol fuel cell has been the subject of intensified recent development because of its high energy density in generating electric power from fuel. This has many benefits in terms of both operating costs and environmental concerns. Adaptation of such cells to mobile uses, however, is not straightforward because of technical difficulties associated with reforming the hydrocarbon fuel in a simple and cost effective manner. Further, a safe and efficient storage means for the hydrogen gas presents a challenge because hydrogen gas must be stored at high pressure and at cryogenic temperatures or in heavy absorption matrixes in order to achieve useful energy densities. It has been found, however, that a compact means for storing hydrogen is in a hydrogen rich compound with relatively weak chemical bonds, such as methanol (and to a lesser extent, ethanol, propane, butane and other hydrocarbons). Thus, the DMFC has been developed.
 Depending upon the application with which the DMFC is ultimately employed, it may be desirable that the cell operate efficiently regardless of physical orientation. As such, the fuel delivery system that supplies the fuel to the cell should be capable of delivering the fuel in a variety of orientations, and independent of the volume of liquid in the system.
 In addition, the components (including the management systems in the DMFC) are minute and subject to clogging if the fuel is in poor, impure or contaminated condition. Components on the anode side of the fuel cell need to remain uncontaminated for proper operation of the cell. Therefore, a very pure fuel must be fed to the anode in order to provide optimal DMFC performance.
 While methanol has many attractive qualities as a fuel, it can be hazardous in certain proportions. In a pure state methanol is colorless and its vapor is virtually odorless. As such, there are numerous regulations and guidelines directing that certain additives be introduced to methanol that is used in commercial products (such as windshield washer fluid used in automobiles). These additives provide certain characteristics such as creating an unpleasant taste, adding smell to methanol vapors, as well as adding color to flame. It is possible, however, that some of these additives would react with an anode catalyst in a direct methanol fuel cell, or have a detrimental effect on the membrane. For example, some of the additives may adhere to the anode, blocking an active portion of the catalyst or otherwise impeding the performance of the anode, and therefore the DMFC.
 It is thus an object of the present invention to provide a fuel storage container and delivery system for a direct oxidation fuel cell that introduces “clean” fuel in the form of is either pure fuel or an aqueous fuel solution to the cell. It is a further object of the invention to provide a delivery system which allows for mixture of additives with the fuel prior to release of the fuel into the environment outside of the system. There remains a need, therefore, for a fuel storage container and delivery system that delivers pure fuel or an aqueous solution to the system while providing the capability of mixing the fuel with additives prior to its release elsewhere.
 It is a further object of the invention to provide a delivery system that continues to supply fuel solution to the system, even while the system is in various orientations.
 The present invention provides a delivery system in a protective multiple-walled fuel assembly for use with a direct oxidation fuel cell system. In one embodiment of the invention, the assembly includes an outer, firm-walled container. An inner tank is disposed entirely within the outer container. A plenum is defined between the outer container and the inner tank. The inner tank holds the fuel, which may be pure fuel or an aqueous fuel solution. The plenum is filled with one or more additive substances which, when mixed with the fuel, provide color, taste, and odor to enhance recognizability of the fuel.
 The delivery system includes a needle such as a hypodermic needle having a hollow central portion. The needle is introduced through an opening in the outer container and pierces the inner tank to draw fuel out of the inner tank for delivery to the direct oxidation fuel cell. The needle withdraws the fuel either under the force of gravity or under pressure provided by a pressure chamber, which can also be disposed within the outer container. A pump may be used to provide suction to draw fuel from the delivery system.
 The assembly thus delivers the fuel to the direct oxidation fuel cell system. However, should the cell or the container be dropped or subjected to force that ruptures the assembly, both the inner tank containing the fuel and the outer container (including the additives) are ruptured. As a further precaution, a coupling agent, which may be a wire or string, can be employed between the inner tank and the outer container to cause rupture or induce rupture of the inner tank in the case that the outer tank ruptures first. Accordingly, this causes mixing of the fuel with the additives, thus providing the safety features of a liquid fuel mixed with additives.
 In accordance with another aspect of the invention, the inner tank is a flexible bladder that is filled with fuel. Again, there is a plenum between the outer container and the flexible bladder which plenum contains the additives. There is also a pressure chamber disposed within the container, which applies pressure to the bladder. The outer container is sealed, and a needle is introduced through the seal to draw out the fuel. The bladder deflates under the applied pressure as the fuel is consumed by the fuel cell. This embodiment exhibits enhanced performance because the shape of the flexible bladder conforms generally to the volume of the liquid it contains. Accordingly, the liquid fuel is accessible to the fuel cell independent of the volume of liquid in the bladder or of the orientation of the assembly.
 In accordance with yet a further aspect of the invention, a safety device is provided on the needle that is introduced into the flexible bladder that serves as the inner tank in this embodiment. When the needle is withdrawn from the flexible bladder, the safety device causes a tear in the bladder that causes the fuel to mix with the additives in the plenum. Accordingly, a safer liquid is provided that can later be more easily disposed of before refilling of the fuel delivery assembly, or disposed of directly in a single usage embodiment.
 The invention description below refers to the accompanying drawings, of which:
FIG. 1 is a block diagram of a direct methanol fuel cell system with which the present invention may be employed;
FIG. 2 is a schematic cross section of one embodiment of the fuel delivery system of the present invention;
FIG. 3A is a schematic side view of the sealing plug that is used in one embodiment of the present invention;
FIG. 3B is a schematic top plan view of the sealing plug of FIG. 3A;
FIG. 4 is an isometric illustration of the fuel container and delivery assembly of one embodiment of the present invention showing a rupture of the assembly;
FIG. 5 is a schematic cross section of the fuel container and delivery assembly of the present invention illustrating the pressure chamber aspect of the assembly;
FIG. 6 is a schematic cross section of a needle containing a safety device to be used in a container and delivery assembly in accordance with the present invention;
FIG. 7A is a schematic cross section of the needle with the safety device as introduced into the flexible bladder of one embodiment of the present invention; and
FIG. 7B is a schematic cross section of the flexible bladder as ruptured in accordance with the present invention.
 The present invention is a fuel storage container and delivery assembly. The fuel may be any hydrocarbon-based fuel including, but not limited to, methanol, ethanol, propane and butane, or an aqueous solution thereof. For purposes of illustration, we herein describe an illustrative embodiment of the invention as it is employed in connection with a direct methanol fuel cell (“DMFC”), with the fuel substance being methanol or an aqueous methanol solution. It should be understood, however, that it is within the scope of the present invention that the fuel container and delivery system can be readily used for other fuels to be stored and delivered to direct oxidation fuel cells. Thus, as used herein, the word “fuel” shall include methanol, ethanol, propane, butane or combinations thereof, and aqueous solutions thereof and other hydrocarbon fuels amenable to use in a direct oxidation fuel cell system.
FIG. 1 shows a direct methanol fuel system 2 with which the fuel delivery system of the present invention may be used. For a better understanding of the present invention, the system 2 will be briefly described. The system 2 contains a direct methanol fuel cell (DMFC) 3 and a fuel delivery system 4 in accordance with the present invention. The direct methanol fuel cell 3 includes a housing 5 which encloses a cathode 6, a membrane electrolyte 8 and an anode 10.
 Methanol or a solution of methanol and water are introduced into the anode side of housing 5 while oxygen (air) is introduced into the cathode side of the housing 5. The source of the oxygen is preferably ambient air but it should be understood that other sources could be used. As a result of the reactions at the anode and cathode, free electrons flow from the anode 10 through a load 12 to the cathode 6, while hydrogen ions flow from the anode 10 through the membrane electrolyte 8 to the cathode 6. So long as the chemical reactions continue, a current is maintained through the load 12.
 Fuel from the fuel delivery system 4 may be used to fill a reservoir 15, from which the fuel will be drawn. Alternatively, fuel may be supplied directly to pump 16, in which case the reservoir 15 is not needed. The pump 16 is coupled to a first gas separator 14, and to the direct methanol fuel cell 3, as well as to gas separator 18. The first gas separator 14 receives effluent from the anode 10 of the fuel cell 3 and separates it into liquid (i.e., unreacted methanol or methanol and water) and carbon dioxide. The liquid component is supplied to the pump 16 for recirculation to the fuel cell 3. The pump 16 creates suction to draw fuel from the fuel delivery system 4. The gas component may also be supplied to pump 16 and may be used to drive the pump in accordance with the teachings of commonly-owned U.S. patent application Ser. No. 09/717,754.
 As noted, it is desirable to introduce only “clean” fuel (in the form of either pure methanol or a methanol/water mixture) into the system 2. Referring to FIG. 2, a fuel delivery assembly 20, which represents one implementation of assembly 4 (FIG. 1) is constructed in accordance with a first embodiment of the present invention. The fuel container and delivery assembly 20 is comprised of a multiple walled-container. More specifically, an inner tank 22 is disposed within an outer container 24. The inner tank 22 contains the pure methanol or an aqueous methanol solution. The inner tank 22 may be constructed from a rigid material, or a semi-rigid material. The outer container 24 is preferably composed of either middle or a high-density, chemically inert plastic. In the embodiment of the invention that is illustrated in FIG. 2, both the inner tank 22 and the outer container 24 are composed of semi-rigid or rigid materials. Materials that may be used include thermoplastic materials, thermoset resins or plastics as well as other workable materials, which may be suitable. The inner tank 22 is mechanically attached to the outer container 24 by brackets 26 or other suitable attachment means.
 A plenum 28, which is defined between the outer container 24 and the inner tank 22, is filled with a mixture containing the desired additives including, but not limited to coloring and flavoring compounds. The additives may be in a paste or liquid form or may consist of microencapsulated solids. The encapsulation material is dissolved by the introduction of methanol upon mixing, thus releasing the additives. Alternatively, microencapsulated foam can be included as the additive mixture, which foam is released when mixed with methanol.
 The inner tank 22 is filled with a solution of methanol or aqueous methanol solution and is sealed. This inner tank 22 is then placed on a first half of the outer container 24. The second half (not shown) of the outer container is placed over the inner tank 22, leaving an opening at one end thereof 29 (FIG. 2). The plenum 28 between the inner tank 22 and the outer container 24 is then filled with desired additives. The outer container 24 is then sealed with a permanent plastic seal 30 or with a plug 32.
 The plug 32 is illustrated in FIG. 3A. A top plan view of the plug 32 is illustrated in FIG. 3B. The plug 32 preferably includes a center portion 34, which is rubber or flexible plastic material. The methanol fuel is removed from the inner tank 22 by inserting a needle 38, which is similar to a hypodermic needle, through the seal 30 or the rubber portion 34 of the plug 32 to penetrate the inner tank 22. The methanol solution is then, by force of gravity, drawn from the inner tank 22 through an aperture 40 in the needle 38 into the reservoir 15 or directly into the direct methanol fuel cell system illustrated in FIG. 1.
 In this fashion, the DMFC 3 is fueled without introducing unnecessary additives into the fuel supply, thus avoiding contamination of the anode or clogging of conduits by the additives.
 The additives, however, will be mixed with the fuel should there be a rupture of the assembly 20. As illustrated in FIG. 4, if a product such as a hand held device (e.g., a mobile telephone or a laptop computer), should be dropped or crushed, the fuel container and delivery assembly 20 breaks, as in the break 40, causing the fuel 44 to escape from inner tank 22. However, in accordance with the invention, as the methanol is released from inner tank 22, it is mixed with additives 48, which are released from the plenum 28. As a further precaution, to guard against the possibility of the outer container rupturing prior to the inner tank, we have provided a coupling device 49 which ruptures the inner tank 22 upon rupture of the outer container 24. In accordance with one aspect of the invention, the rupture device 49 is a wire or string that provides tension on the inner tank 22 to rupture it when the outer container 24 ruptures.
FIG. 5 illustrates another embodiment of the invention. An outer container 54 is a housing preferably fabricated from a plastic or metal. An inner tank 56 is a flexible bladder, which is fully expanded by filling it with a fuel. It may be composed of a plastic resin that is capable of being pierced by a needle. The inner tank 56 may also be a semirigid, preferably collapsible container, if desired, but it is referred to for purposes of this description as a flexible bladder. Within the outer container 54, a separate chamber 60 is filled with gas at a higher pressure than the remainder of the area within the outer container 54. The chamber 60 is integrated into or mechanically attached to the outer container 24. Alternatively, a small area of the enclosure within the outer container 54 is physically segregated from the remainder, and a higher pressure is created within this small area. The gas in the chamber 60 is released very slowly by way of a flow-limiting orifice 64. The higher pressure within the chamber thus compresses the flexible bladder 56 to force the fuel into the DMFC as needed.
 The outer container 54 is sealed with a seal or plug 70. As illustrated in FIG. 6, a guide 72 houses a needle 74. The guide 72 provides sufficient tension to allow the needle 74 to puncture the seal 70 as well as the flexible bladder 56 in order to draw fuel from bladder 56 into the DMFC. The guide 72 and needle 74 may be suitably connected to either the DMFC or the assembly including outer container 54, as desired in the particular application. A valve in the container or which may be within the DMFC (not shown) may be desirable for controlling the flow of fuel as will be understood by those skilled in the art. It may be further desirable to shape the external tank as shown in FIG. 5 with sloped sides 76 in a way that funnels the fuel into the DMFC.
 As illustrated in FIGS. 7A and 7B, in which like components have the same reference characters as in the earlier described figures, the guide 72 houses needle 74. The fuel container and delivery assembly includes flexible bladder 56, which contains fuel. The plenum 68, which is defined between the outer container 54 and the flexible bladder 56, is filled with additives. The needle 74 is introduced into the opening 29 of the outer container 54 and pierces the inner flexible bladder 56. In operation, the fuel is then drawn out of the assembly and fed as the fuel supply to the associated DMFC.
 It is highly desirable to provide that any unused methanol remaining in the assembly be mixed with the additives prior to its disposal or release from the fuel delivery assembly. As such, we have provided in this embodiment of the invention a safety device 80 on the needle 74. As illustrated in FIG. 7B, when the needle and housing are removed from the fuel delivery assembly, in the direction of the arrow, this causes a tear in the flexible bladder 56. The methanol solution is then released from the bladder 56. As it is released from the bladder 56, it mixes with the additives contained in the plenum 68. An external seal or plug 88 is used to ensure that the methanol solution and additive mixture does not escape from the external tank 54 into the environment. The plug 88 is preferably constructed of a dense self-sealing material that substantially resists the additives and methanol solution from being released.
 After the fuel supply is exhausted, the tank (now containing the mixture) can thereafter be emptied and a new flexible bladder can be introduced into the tank filled with methanol. Then, the plenum is refilled with additives and the tank is resealed. Alternatively, it may be desirable to provide a disposable assembly in a single usage embodiment in which case the liquid disposed of includes the additives.
 As stated, it should also be understood that the present invention can also be readily employed with fuels other than methanol or methanol/water mixtures. Also, as noted, the additives may be placed within the inner tank, and the fuel disposed within the outer container if preferred in a particular application.
 The foregoing description has been directed to specific embodiments of the invention. It will be apparent, however, that other variations and modifications may be made to the described embodiments, with the attainment of some or all of the advantages of such. Therefore, it is the object of the appended claims to cover all such variations and modifications as come within the true spirit and scope of the invention.
 What is claimed is:
|Citing Patent||Filing date||Publication date||Applicant||Title|
|US7105245||Jul 2, 2003||Sep 12, 2006||Neah Power Systems, Inc.||Fluid cell system reactant supply and effluent storage cartridges|
|US7115335||Oct 29, 2004||Oct 3, 2006||Entegris, Inc.||Connector assembly for fluid transfer|
|US7205060||Jul 29, 2005||Apr 17, 2007||Ultracell Corporation||Method and system for controlling fluid delivery in a fuel cell|
|US7276096||Jun 25, 2004||Oct 2, 2007||Ultracell Corporation||Fuel processor dewar and methods|
|US7291191||Sep 16, 2005||Nov 6, 2007||Ultracell Corporation||Fuel cell cartridge filters and pressure relief|
|US7401712||Sep 16, 2005||Jul 22, 2008||Ultracell Corporation||Smart fuel cell cartridge|
|US7462208||Jun 25, 2004||Dec 9, 2008||Ultracell Corporation||Planar micro fuel processor|
|US7585581||Jul 30, 2007||Sep 8, 2009||Ultracell Corporation||Micro fuel cell architecture|
|US7604673||Jun 25, 2004||Oct 20, 2009||Ultracell Corporation||Annular fuel processor and methods|
|US7625655||Aug 15, 2007||Dec 1, 2009||The Gillette Company||Fuel container and delivery apparatus for a liquid feed fuel cell system|
|US7638214||May 25, 2005||Dec 29, 2009||The Gillette Company||Fuel cells|
|US7638215||Nov 8, 2005||Dec 29, 2009||Mti Microfuel Cells Inc.||Method of controlling delivery of fuel to a direct oxidation fuel cell|
|US7648792||May 2, 2006||Jan 19, 2010||Ultracell Corporation||Disposable component on a fuel cartridge and for use with a portable fuel cell system|
|US7655337||Jun 25, 2004||Feb 2, 2010||Ultracell Corporation||Micro fuel cell thermal management|
|US7666539||Dec 20, 2005||Feb 23, 2010||Ultracell Corporation||Heat efficient portable fuel cell systems|
|US7763368||Jun 25, 2004||Jul 27, 2010||Ultracell Corporation||Efficient micro fuel cell systems and methods|
|US7767351||Nov 13, 2009||Aug 3, 2010||The Gillette Company||Fuel cell with cartridge and colorant|
|US7807313||May 2, 2005||Oct 5, 2010||Ultracell Corporation||Compact fuel cell package|
|US7935452||Dec 31, 2008||May 3, 2011||Ultracell Corporation||Micro fuel cell architecture|
|US7943263||Jul 30, 2007||May 17, 2011||Ultracell Corporation||Heat efficient portable fuel cell systems|
|US8043757||Dec 24, 2008||Oct 25, 2011||UltraCell Acquisition Company, L.L.C.||Efficient micro fuel cell systems and methods|
|US8318368||Aug 6, 2007||Nov 27, 2012||UltraCell, L.L.C.||Portable systems for engine block|
|US8821832||Dec 5, 2011||Sep 2, 2014||UltraCell, L.L.C.||Fuel processor for use with portable fuel cells|
|US20040096721 *||Jul 2, 2003||May 20, 2004||Ohlsen Leroy J.||Closed liquid feed fuel cell systems and reactant supply and effluent storage cartridges adapted for use with the same|
|US20040173615 *||Mar 7, 2003||Sep 9, 2004||Goodman John B.||Fuel storage container for a fuel cell|
|US20050005521 *||Jun 25, 2004||Jan 13, 2005||Ultracell Corporation||Fuel processor dewar and methods|
|US20050008909 *||Jun 25, 2004||Jan 13, 2005||Ultracell Corporation||Efficient micro fuel cell systems and methods|
|US20050008911 *||Jun 25, 2004||Jan 13, 2005||Ultracell Corporation||Micro fuel cell thermal management|
|US20050011125 *||Jun 25, 2004||Jan 20, 2005||Ultracell Corporation, A California Corporation||Annular fuel processor and methods|
|US20050014059 *||Jun 25, 2004||Jan 20, 2005||Ultracell Corporation||Micro fuel cell architecture|
|US20050022448 *||Jun 25, 2004||Feb 3, 2005||Ultracell Corporation||Planar micro fuel processor|
|US20050147864 *||Oct 29, 2004||Jul 7, 2005||Eggum Shawn D.||Connector assembly for fluid transfer|
|US20050181271 *||Mar 17, 2005||Aug 18, 2005||Xiaoming Ren||Simplified direct oxidation fuel cell system|
|US20050186455 *||Jun 25, 2004||Aug 25, 2005||Ultracell Corporation, A California Corporation||Micro fuel cell system start up and shut down systems and methods|
|US20050255368 *||May 11, 2005||Nov 17, 2005||Ultracell Corporation, A California Corporation||High surface area micro fuel cell architecture|
|US20060006108 *||Jul 7, 2005||Jan 12, 2006||Arias Jeffrey L||Fuel cell cartridge and fuel delivery system|
|US20060014069 *||Sep 16, 2005||Jan 19, 2006||Ultracell Corporation||Smart fuel cell cartridge|
|US20060029848 *||Jul 29, 2005||Feb 9, 2006||Ultracell Corporation||Method and system for controlling fluid delivery in a fuel cell|
|US20090269647 *||Nov 11, 2005||Oct 29, 2009||Toyo Seikan Kaisha, Ltd.||Cartridge for methanol fuel cell|
|DE10348879B4 *||Oct 21, 2003||Jun 6, 2007||Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V.||Vorrichtung und Verfahren zur Erhöhung der Brennstoffkonzentration in einem der Anode einer Brennstoffzelle zugeführten, einen Brennstoff enthaltenden Flüssigkeitsstrom und deren Verwendung|
|EP1176650A2 *||Jul 19, 2001||Jan 30, 2002||Alcatel Alsthom Compagnie Generale D'electricite||System for storing fuel in a handheld device|
|EP1331684A2 *||Jan 8, 2003||Jul 30, 2003||Hewlett-Packard Company||Fuel supply for a fuel cell|
|EP1416551A2 *||Sep 30, 2003||May 6, 2004||Hewlett-Packard Development Company, L.P.||Protective container with preventative agent therein|
|EP1464091A1 *||Dec 20, 2002||Oct 6, 2004||MTI Microfuel Cells, Inc.||Fuel container and delivery apparatus for a liquid feed fuel cell system|
|EP1476238A1 *||Feb 18, 2003||Nov 17, 2004||MTI Microfuel Cells, Inc.||Simplified direct oxidation fuel cell system|
|EP2161775A1 *||Feb 2, 2005||Mar 10, 2010||Mitsubishi Pencil Co., Ltd.||Fuel battery and fuel storage for fuel battery|
|WO2005004268A1 *||Jun 21, 2004||Jan 13, 2005||Satosi Komiyama||Fuel container for fuel cell|
|WO2006010012A2 *||Jul 7, 2005||Jan 26, 2006||Direct Methanol Fuel Cell Corporation||Fuel cell cartridge and fuel delivery system|
|WO2006127201A2 *||Apr 26, 2006||Nov 30, 2006||Gillette Co||Fuel cells|
|U.S. Classification||422/40, 206/524.4, 222/82|
|Cooperative Classification||Y02E60/50, H01M8/04186, H01M8/04208, H01M8/1011|
|European Classification||H01M8/04C4, H01M8/04C6B|
|Feb 20, 2001||AS||Assignment|
|May 30, 2001||AS||Assignment|
|Sep 30, 2004||AS||Assignment|
|Oct 5, 2005||AS||Assignment|
Owner name: THE GILLETTE COMPANY, MASSACHUSETTS
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:MTI MICROFUEL CELLS INC.;REEL/FRAME:017065/0680
Effective date: 20040922
|Mar 28, 2006||FPAY||Fee payment|
Year of fee payment: 4
|Mar 23, 2010||FPAY||Fee payment|
Year of fee payment: 8
|Mar 26, 2014||FPAY||Fee payment|
Year of fee payment: 12