EP1726058A1 - Pile a combustible composee de capillaires - Google Patents

Pile a combustible composee de capillaires

Info

Publication number
EP1726058A1
EP1726058A1 EP05731207A EP05731207A EP1726058A1 EP 1726058 A1 EP1726058 A1 EP 1726058A1 EP 05731207 A EP05731207 A EP 05731207A EP 05731207 A EP05731207 A EP 05731207A EP 1726058 A1 EP1726058 A1 EP 1726058A1
Authority
EP
European Patent Office
Prior art keywords
fuel cell
cell according
capillaries
segments
fuel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP05731207A
Other languages
German (de)
English (en)
Inventor
Stephan Rüdiger BLUM
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
White Fox Technologies Ltd
Original Assignee
White Fox Technologies Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by White Fox Technologies Ltd filed Critical White Fox Technologies Ltd
Publication of EP1726058A1 publication Critical patent/EP1726058A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1009—Fuel cells with solid electrolytes with one of the reactants being liquid, solid or liquid-charged
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90—Selection of catalytic material
    • H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
    • H01M4/9025—Oxides specially used in fuel cell operating at high temperature, e.g. SOFC
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
    • H01M8/1213—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte characterised by the electrode/electrolyte combination or the supporting material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465—Details of groupings of fuel cells
    • H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1009—Fuel cells with solid electrolytes with one of the reactants being liquid, solid or liquid-charged
    • H01M8/1011—Direct alcohol fuel cells [DAFC], e.g. direct methanol fuel cells [DMFC]
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465—Details of groupings of fuel cells
    • H01M8/247—Arrangements for tightening a stack, for accommodation of a stack in a tank or for assembling different tanks
    • H01M8/2475—Enclosures, casings or containers of fuel cell stacks
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells

Definitions

  • the invention relates to a fuel cell, in particular a direct methanol fuel cell.
  • WO 00/54358 explains the structure of fuel cell modules, in each of which a large number of individual microreactors are arranged in a frame in a plane and connected in series.
  • the surfaces of the individual electrodes, which are designed as cathodes, are in direct contact and the coaxial inner anodes of the individual microreactors are connected to one another on one end of the module.
  • Individual modules of this type can in turn be connected in series and / or in series.
  • the built-up electrical potential is regularly tapped off axially at the end of the microreactor. It also determines the length of the microreactor and the electrical performance. If so-called tubular assemblies are used in particular as microreactors, the mechanical stability is regularly low and the length of such a microreactor is therefore limited and the power yield or the level of the voltage which can be tapped off is correspondingly low.
  • the object of the invention is to provide a fuel cell which ensures a high power yield with a structurally simple structure, combined with low development costs.
  • the capillaries are arranged in adjoining segments in bundles m each within a reaction space that the electrode is led out at both ends of each capillary that the
  • Electrodes of the capillaries of a segment are electrically connected at essentially the same potential on both ends and that at least one wall section of each segment is provided with a counter electrode or at least forms it.
  • the fuel cell according to the invention has a number of advantages.
  • the capacity of the fuel cell is determined by the number of segments, which are regularly constructed in the same way and can be produced in series, as it were. It is essential that the coaxial structure of the known microreactors is left, which means that the length of the capillaries is no longer decisive for the voltage potential between the first and second electrodes. Rather, each capillary has only one Electrode, which is connected in parallel at both ends to the corresponding electrodes of the remaining capillaries of a segment. Thus, at the end of the capillaries, essentially the same electrical potentials are present at the electrodes against a counterelectrode, which are at or through a
  • Wall section of each segment is formed and which is largely subject to change in shape.
  • the segments can have any cross sections, for example rectangular or triangular.
  • the segments are preferably designed as circular segments in a cross section, which ensures an extremely compact structure, in particular within a cylindrical housing.
  • the electrodes of the capillaries of one segment are connected to the counterelectrode of an adjacent segment, corresponding to a series connection.
  • the electrodes of all capillaries of a fuel cell are connected together at the ends, corresponding to a parallel connection.
  • connection — in parallel or in series — can be predetermined by a switch, in particular an electronic one.
  • a switch in particular an electronic one.
  • each segment has walls which are formed for themselves, in a cross section closed and encircling in a ring shape Enclosing electrodes and consequently forming two spaced partitions between two adjacent segments.
  • These walls which are electrically conductive, can also be used as counter electrodes. Due to the spacing, electrical insulation is regularly not necessary. However, the formation of two spaced-apart partitions between two adjacent sectors can also be expedient whenever an inactive region of an electrolyte is to be created between these partitions.
  • Partitions then regularly have a specially designed counter electrode.
  • partitions can be made leaky, to the extent that partitions are provided with openings which correspond to one another, in particular when two partitions are formed, directly opposite one another.
  • elaborate sealing measures are also avoided in the case of common partition walls and an exchange of an electrolyte or the like is also possible under the segments.
  • a common partition wall of two adjacent segments has a counterelectrode on both sides, each assigned to one of the segments.
  • Each segment of circular cross-section therefore has two diagonally opposite counter electrodes.
  • a counter electrode has a carrier plate j which is covered with a grid-like holder for a catalyst.
  • a grid-like holder 3-cann be an expanded metal, a metal grid, a metal mesh or a comparable porous material, on or in which a catalyst of crystalline structure easily finds a hold.
  • the kajpillare also preferably has a lattice-like core covered with a catalyst, which is surrounded in a ring by a membrane.
  • a wide variety of versions of the capiZLlare are possible, as described, for example, in WO 02/15318.
  • the core, the carrier plate and / or the grid-like holder are made of titanium.
  • a flow through the capillaries is open and freely accessible at the end. That this means that the ends of the capillaries penetrate housing walls, head plates or the like delimiting both ends of the functional spaces of the segments and remain open in front of these.
  • a fuel cell is then provided for air to flow through the capillaries and for a pressure space in one end of the capillaries to be formed by a housing in which the capillaries end openly and which is supplied with ambient air by means of a fan.
  • a gas can be pressed as a fuel component under high pressure by the capillaries, but such a pressurized fuel component is not available everywhere.
  • the small pressure difference that is built up by the fan is advantageously sufficient to conduct air through the capillaries.
  • a common, closed-ended supply line for a fuel component is provided between adjacent edges or tips of segments and that the supply line in reaction spaces of the segments with
  • the supply line provides a central supply of several to all of the reaction spaces of a fuel cell with a fuel component, the supply line at least partially limiting such a reaction space, in particular at least forming the edges or tips thereof.
  • An exhaust pipe is designed to be comparable, which has openings for one in the reaction spaces of the segments
  • the exhaust gas line is expediently also formed centrally and is in particular a continuation of the supply line. However, naturally both lines are closed off from one another.
  • At least one pump is connected to the supply line and that the pump is arranged in a pump space of a housing opposite the pressure space, thus the reaction spaces are arranged between the pressure space and the pump space.
  • the pressure build-up by the pump within the supply line must be dimensioned such that the inlet the fuel component is placed in the reaction spaces.
  • This pump is expediently arranged in a pump chamber of a housing opposite the pressure chamber, whereby the fuel cell according to the invention has an extremely compact, longitudinally oriented design.
  • the fuel component introduced into the reaction spaces through the supply line is a fuel mixture
  • individual components of the fuel mixture can each be fed into the supply line by means of a controllable pump, a control device regulating the pumps in an optimally setting the proportions of the individual components in the fuel mixture.
  • a fuel mixture of water and methanol is particularly intended and the fuel cell according to the invention is preferably operated as a direct methanol fuel cell.
  • the fuel cell according to the invention is largely designed as an open system and can therefore be dispensed with many pressure-tight connections.
  • a liquid phase emerging from the capillaries for example condensed water or the like, if necessary.
  • a combustion product can be collected and discharged in an underside catchment area, if necessary. after processing, the combustion process can also be re-introduced.
  • the reaction spaces are filled with acidic methanol, but preferably above the liquid level the acidic methanol remains a free space in which a gaseous combustion residue, for example C0 2 , can collect and from there is discharged to the outside via the exhaust pipe.
  • a gaseous combustion residue for example C0 2
  • the fill level of the reaction spaces is monitored accordingly with fill level sensors, so that a fill level that is too high and too low is reliably detected. If this occurs, the " combustion process in the fuel cell is expediently prevented.
  • the segments are arranged within a cylindrical housing and that the housing is closed axially by head plates penetrated by the capillaries.
  • the electrodes of the capillaries are also electrically connected by the head plates.
  • the head plates are also provided with separating bars, picking up the arrangement of the partition walls of the sectors, between which a filling is arranged encompassing the capillaries of the underlying sector.
  • the filling can hold separately formed walls of the sectors, for example against the separating bars, and the electrical connections of the counterelectrodes are preferably led out of the sectors through the head plates and also connected via the same.
  • the top plates preferably have grooves on their sides axially closing the reaction spaces for receiving the partition walls.
  • the partition walls are held securely without major design measures. As explained at the beginning, further sealing measures are not necessary.
  • a partition wall has two protruding connection pieces, which are provided on both sides with an attachment of the carrier plate, both of which penetrate the head plates that axially close the housing.
  • the housing is provided with flanges for connecting the pressure chamber housing and the oppositely arranged rooms.
  • the pressure chamber can be closed off from the environment in a simple manner by a pressure chamber housing of cover-like design.
  • Fig. 1 shows a cylindrical housing 1 in which. six segments 2-7 mi, which adjoin one another in the same way: a multiplicity of capillaries 8 flowing through and / or through a fuel component are provided, each arranged in bundles, cf. FIG. 3.
  • the capillaries 8 have a cloverleaf profile 9 lying radially on the inside, which is encased by a grid-like structure as an electrode 10, which in turn is provided on the radially outside with a catalyst 11.
  • a Membrane 12 completes the construction of a capillary 8 lying radially on the outside. Since the profile 9 is made of an electrically conductive material that supports the capillary 8, in particular of a metal such as preferably titanium, the electrical potential can be tapped from the grid-like structure as well as from the profile 9 itself as the electrode 10 led out at both ends.
  • the electrodes 10 or here also the profiles 9 of each segment 2 to 7 are connected in parallel at both ends, essentially also at the same electrical potential, for example shown in FIG. 3 for the segments 3, 5 and 7.
  • each segment has 2 to 7 walls 13 to 18 which are formed by themselves, ring-shaped in the view according to FIG. 3 revolving around the capillaries 8 of each segment 2-7, so that two spaced partition walls 19, 20 are formed, for example, between the segments 5 and 6, cf. also Fig. 6.
  • the electrically conductive walls 13 to 18 themselves form the counter electrodes and show the segments 3, 5, 7 in FIG. 3 an interconnection of the electrodes 10 of the capillaries 8 of the segments 3, 5, 7 connected in parallel to connecting webs of the walls 13 designed as counter electrodes , 15, 17 of the respectively adjacent segments 2, 4 and 6.
  • the housing 1 is axially closed at both ends by head plates 21, 22 which are penetrated by the capillaries 8 and which end openly and freely.
  • the top plates 21, 22, of the same design take up the arrangement of the partitions 19, 20 between adjacent segments 5, 6 and are also provided with spoke-like partitions 23, 24. Between the dividers 23, 24 and an outer ring of the head plate 21 edged, the wall 16 passes through the head lath 21 with an exact fit.
  • An underlying reaction space is axially closed by a filling 25 enclosing and holding the capillaries 8.
  • the walls 13-18 of the segments 2-7 of the head plates 21, 22 are held at a distance from the inner wall 96 of the housing 1.
  • the two partition walls 26, 27 formed between the individual segments 2 to 7, like the others, see FIG. 5, are preferably provided with opposite openings 28, 29, so that an electrolyte flows within the housing 1 and the segments 2-7 is largely possible.
  • FIG. 7 is of a substantially cylindrical shape. The reaction takes place within a cylindrical housing 31, see also FIG. 13, which is provided at the end with flanges 32, 33 for further attachments.
  • the fuel cell 30 is again a variety of
  • the capillaries 34 of the same design have a coiled core as the electrode 41, but a tube-like one is preferred, the jacket of which has a grid-like design and is coated with a catalyst and which consists of a
  • the electrode is surrounded in a ring by a membrane 42.
  • this electrode represents a cathode.
  • the souls of the capillaries 34, as electrodes 41, are electrically connected in parallel at both ends in this exemplary embodiment, essentially at the same potential.
  • the electrodes 41 of a segment 35-40 are connected in parallel at both ends and in each case against the same counterelectrodes, in the operating mode described here, the anodes of adjacent segments.
  • the segments 35 to 40 are separated from one another in a spoke-like manner by common partition walls 43, 44, see FIG. 9, sealing measures being unnecessary.
  • the partition wall 45 shown in FIG. 12 is provided on both sides with counter electrodes 46, 47 of the same type on an electrically non-conductive core 58.
  • the counter electrode 46 has on a carrier plate 48 a grid-like holder 49 for a catalyst, which consists in particular of an expanded metal or a fabric made of titanium.
  • each bundle of capillaries 34 becomes one
  • Segments 35-40 each bordered by two diagonally opposite counter electrodes.
  • the partition walls 45 have opposite, axially projecting ones and connection pieces 52, 53 provided on both sides with a shoulder 50, 51 of the carrier plate 48.
  • the partitions 45, together with the capillaries 34, are held in head plates 54, 55 and penetrate them.
  • the head plates 54, 55 are also provided with grooves 56, 57 in the manner of spokes.
  • the connecting pieces 53 of the electrodes 46, 47 are led out through rectangular openings 59, cf. Fig. 11.
  • FIGS. 9 and 10 show that the capillaries 34 also penetrate the head plates 54, 55 and protrude openly therefrom.
  • the electrodes 41 and / or the connecting pieces of the counter electrodes are connected by means of head pieces 93, 94 designed as circuit boards, cf. the connecting pieces 86-89 of the partition walls 43, 44 according to the section in FIG. 9.
  • the capillaries 34 which are open at the ends, can be flowed through by a gas, here air.
  • a pressure chamber 60 is formed at the upper end of the capillaries.
  • a fan 61 under an opening 80 in the pressure chamber housing 81 provides, albeit slight, overpressure in the pressure chamber 60 with respect to the ambient pressure. However, this is completely sufficient for air to flow through the capillaries 34, which then emerges in a space 62 and escapes into the environment via openings 63 in a housing 64.
  • the pressure chamber housing 81 is hat-shaped and is fixed against the upper flange 32 of the housing 31, whereby customary sealing measures in the form of an O-ring 95 can also be provided.
  • the space 62 can also serve as a collecting space for a liquid phase 65 emerging from the capillaries 34, for example condensation here, but also for a possible one Combustion product in a differently configured fuel cell. Sometimes. For this purpose, an additional collecting space can also be provided below space 62.
  • the condensed water can be disposed of or alternatively, if necessary. after reprocessing, can be reintroduced into the combustion cycle as a fuel component.
  • a fuel mixture consisting of water and methanol is used in the fuel cell 30.
  • This fuel mixture is fed via a common, closed-ended supply line 66 to reaction spaces 68, 69 of the segments, for which purpose the supply line 66 is provided with openings 67 and also forms the tips of the segments.
  • the reaction spaces 68, 69 are filled with acidic methanol 70, 71 as the electrolyte. So that the fuel mixture now safely reaches the reaction spaces 68, 69, a pump 72, 73 is provided in a pump space 75 for each fuel component, water and methanol. While methanol enters the system from the outside via a connecting piece 74, the liquid phase 65, if water, but in particular water from a specially designed tank, for example in a room 76, can be fed to the combustion process.
  • the pump chamber 75 is arranged opposite the pressure chamber 60, so that these two chambers 75, 60 enclose the housing 31 with the reaction chambers located therein between them.
  • a control device which is provided in a further space 77, can optimally adjust the proportions of the individual components, here of water and methanol, of the fuel mixture by regulating the pumps 72, 73.
  • the spaces 62, 75, 76 and 77 are set into one another in a box-like manner and braced against the lower flange 33 of the housing 31 by means of an end plate 78 and here four screws 79. Additional rooms or fans for cooling the electronics of the control system can be connected due to the construction principle. Sometimes.
  • a further fuel cell can also be connected, but then a sufficient distance must be provided so that air can enter the pressure chamber 60 through the opening 79 in the pressure chamber housing 81.
  • the fuel cell 30 is designed for operation with only vertically rising capillaries and an overhead pressure chamber 60. Since the acidic methanol 70.71 does not fill the reaction spaces 68.69 up to the top plate 54, a free space 82.83 remains in each case above the acidic methanol 70.71. Gaseous reaction products, here in the form of CO 2 , collect in these free spaces 82, 83 and are released into the open via an exhaust line 84 provided with openings 85.
  • the exhaust line 84 continues the supply line 66 centrally between the adjacent tips of the segments and forms the walls of the supply line 66 and the
  • Exhaust line 84 has a boundary of the reaction spaces 67, 68. However, no special sealing measure is required either between the common partition walls 43, 44 and the supply line 66 or exhaust line 84.
  • level sensors 90 to 93 are also provided, which monitor the fill level of the methanol 70.71 in the reaction spaces 68.69. Since the partition walls 43, 44 are inserted "leaking", it is sufficient to monitor the level of a single reaction space 68. This ensures that the free spaces 83.84 are present above the acidic methanol 70.71 or that there is a sufficient fill level. If one or the other limit is exceeded, the combustion process of the fuel cell is suspended.
  • Exemplary embodiment of a fuel cell according to the invention again shows six sectors 100-105, each with bundles of capillaries 106.
  • sectors 100-105 are separated from one another by two partition walls, for example, sectors 100 and 101 by the two parallel partitions 107, 108.
  • a space 109 filled with an electrolyte remains between the pairs of partition walls 107, 108.
  • This space 109 is accessible via opposite openings 110, 111 in the partition walls 107, 108, with which the reaction spaces 112, 113 of the two sectors 100, 101 are also connected.
  • Each partition 107, 108 is provided with a counter electrode of the type explained in the introduction.
  • Capillaries 206 and connecting pieces 114 of the partition walls 107, 108 have end plates 115 penetrating through them at the ends and freely ending in them, like the section through a pressure chamber housing 116 according to FIG. 15 shows.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Materials Engineering (AREA)
  • Fuel Cell (AREA)

Abstract

L'invention concerne une pile à combustible composée d'une pluralité de capillaires (34) présentant chacun une électrode (41), capillaires sur lesquels et/ou à travers lesquels passe un composant combustible. Ladite invention se caractérise en ce que ces capillaires sont placés en faisceaux dans des segments adjacents (35-40) à l'intérieur d'une chambre de réaction (68, 69) et l'électrode (41) sort des deux extrémités de chaque capillaire. Les électrodes (41) des capillaires (34) d'un segment (35-40) sont connectées électriquement aux deux extrémités de façon à se trouver à un potentiel sensiblement identique et au moins une section de paroi (45) d'un segment (35-40) est pourvue d'une contre-électrode (46, 47) ou constitue au moins cette dernière.
EP05731207A 2004-03-03 2005-03-01 Pile a combustible composee de capillaires Withdrawn EP1726058A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102004010995A DE102004010995A1 (de) 2004-03-03 2004-03-03 Brennstoffzelle
PCT/DE2005/000350 WO2005086270A1 (fr) 2004-03-03 2005-03-01 Pile a combustible composee de capillaires

Publications (1)

Publication Number Publication Date
EP1726058A1 true EP1726058A1 (fr) 2006-11-29

Family

ID=34877477

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05731207A Withdrawn EP1726058A1 (fr) 2004-03-03 2005-03-01 Pile a combustible composee de capillaires

Country Status (9)

Country Link
US (1) US7989114B2 (fr)
EP (1) EP1726058A1 (fr)
JP (1) JP2007526604A (fr)
CN (1) CN100511805C (fr)
BR (1) BRPI0508439A (fr)
CA (1) CA2558496C (fr)
DE (2) DE102004010995A1 (fr)
RU (1) RU2359368C2 (fr)
WO (1) WO2005086270A1 (fr)

Families Citing this family (1)

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Publication number Priority date Publication date Assignee Title
US20140193671A1 (en) * 2013-01-04 2014-07-10 Lilliputian Systems, Inc. Portable Fuel Cell System Having a Fuel Cell System Controller

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DE19517425C1 (de) 1995-05-12 1996-10-17 Mtu Friedrichshafen Gmbh Brennstoffzellenanordnung mit röhrenförmigen Brennstoffzellen
AU3376697A (en) * 1996-06-05 1998-01-05 Southwest Research Institute Cylindrical proton exchange membrane fuel cells and methods of making same
DE19909930B4 (de) * 1999-03-06 2004-09-02 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Herstellung von tubulären PEM-Brennstoffzellen und Ionentauschermembranen
DE19951687A1 (de) 1999-10-27 2001-05-10 Fraunhofer Ges Forschung Polymerelektrolytmembran-Brennstoffzelle
EP1316119A4 (fr) * 2000-07-24 2009-02-11 Microcell Corp Dispositifs et ensembles electrochimiques a microcellules et leur procede de production et d'utilisation
DE10040282A1 (de) 2000-08-14 2002-03-07 Robert Heggemann Brennstoffzelle
US20020197520A1 (en) * 2001-06-25 2002-12-26 Usf Filtration & Separations Group., Inc Micro fuel cell array
DE10132078A1 (de) 2001-07-05 2003-01-23 Stephan Blum Elektrodenanordnung
FR2828013B1 (fr) * 2001-07-24 2003-09-12 Commissariat Energie Atomique Pile a combustible miniature a geometrie cylindrique
US8709674B2 (en) * 2005-04-29 2014-04-29 Alberta Research Council Inc. Fuel cell support structure

Non-Patent Citations (1)

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Title
See references of WO2005086270A1 *

Also Published As

Publication number Publication date
WO2005086270A1 (fr) 2005-09-15
DE102004010995A1 (de) 2005-09-22
BRPI0508439A (pt) 2007-07-24
US20080096065A1 (en) 2008-04-24
JP2007526604A (ja) 2007-09-13
DE112005001017A5 (de) 2007-05-24
RU2006134627A (ru) 2008-06-10
US7989114B2 (en) 2011-08-02
CA2558496C (fr) 2014-01-14
WO2005086270A8 (fr) 2006-11-30
CN100511805C (zh) 2009-07-08
CA2558496A1 (fr) 2005-09-15
RU2359368C2 (ru) 2009-06-20
CN1947300A (zh) 2007-04-11

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