WO2009078866A1 - Fuel cell systems and methods involving variable numbers of flow field passes - Google Patents

Fuel cell systems and methods involving variable numbers of flow field passes Download PDF

Info

Publication number
WO2009078866A1
WO2009078866A1 PCT/US2007/087882 US2007087882W WO2009078866A1 WO 2009078866 A1 WO2009078866 A1 WO 2009078866A1 US 2007087882 W US2007087882 W US 2007087882W WO 2009078866 A1 WO2009078866 A1 WO 2009078866A1
Authority
WO
WIPO (PCT)
Prior art keywords
channels
fuel cell
flow field
manifold
fluid
Prior art date
Application number
PCT/US2007/087882
Other languages
French (fr)
Inventor
Paravastu Badrinarayanan
Sitaram Ramaswamy
Original Assignee
Utc Power Corporation
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 Utc Power Corporation filed Critical Utc Power Corporation
Priority to PCT/US2007/087882 priority Critical patent/WO2009078866A1/en
Publication of WO2009078866A1 publication Critical patent/WO2009078866A1/en

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/02Details
    • H01M8/0202Collectors; Separators, e.g. bipolar separators; Interconnectors
    • H01M8/0258Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465Details of groupings of fuel cells
    • H01M8/2483Details of groupings of fuel cells characterised by internal manifolds
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04313Processes for controlling fuel cells or fuel cell systems characterised by the detection or assessment of variables; characterised by the detection or assessment of failure or abnormal function
    • H01M8/04537Electric variables
    • H01M8/04604Power, energy, capacity or load
    • H01M8/04619Power, energy, capacity or load of fuel cell stacks
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04746Pressure; Flow
    • H01M8/04753Pressure; Flow of fuel cell reactants
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Definitions

  • the disclosure generally relates to fuel cells.
  • Some fuel cell systems are designed to operate at both high power and low power ranges.
  • flow fields of fuel cell systems optimized for high power operation tend to exhibit instability during low power operation. This may be caused due to lower fluid flow velocities and consequent water hang-up within channels of the flow fields, for example.
  • high power operation tends to result in increased parasitic loads and system complexity.
  • an exemplary embodiment of a fuel cell system comprises: a fuel cell flow field having sets of channels operative to route fluid; the flow field being operative such that, in a first mode, fluid is routed through the sets of channels in a first number of passes and, in a second mode, fluid is routed through the sets of channels in a different number of passes.
  • An exemplary embodiment of a fuel cell comprises: a flow field having a first set of channels, a second set of channels, a first manifold assembly and a second manifold assembly, the first set of channels extending between and communicating with the first manifold assembly and the second manifold assembly, the second set of channels extending between and communicating with the first manifold assembly and the second manifold assembly; the flow field being operative such that, in a first mode, fluid is routed from the first manifold assembly to the first set of channels and the second set of channels and, in a second mode, fluid is routed from the first manifold assembly to the first set of channels, through the second manifold assembly, and thereafter to the second set of channels.
  • An exemplary embodiment of a method for operating a fuel cell comprises: operating a flow field of a fuel cell with a first number of passes; and dynamically altering the flow field such that the flow field uses a different number of passes.
  • FIG. 1 is a schematic diagram partially depicting an exemplary embodiment of a fuel cell system.
  • FIG. 2 is a schematic diagram depicting the fuel cell system of FIG. 1 , showing detail of the flow field.
  • FIG. 3 is a schematic diagram of the embodiment of FIG. 1 being operated at a low power level.
  • FIG. 4 is the schematic diagram depicting another embodiment of a fuel cell system being operated at a low power level.
  • FIG. 5 is a schematic diagram depicting the embodiment of FIG. 4 being operated at a high power level.
  • Fuel cell systems and methods involving variable numbers of passes are provided.
  • several embodiments incorporate the use of manifold assemblies that can be dynamically altered to vary the number of passes through a flow field.
  • one or more valves can be selectively positioned such that a multi-pass configuration is provided.
  • the valves can be repositioned to operate the flow field with fewer passes.
  • the flow field can be operated as a single-pass flow field.
  • fuel cell system 100 is configured as a Proton Exchange Membrane (PEM) fuel cell incorporating a membrane 102 that is oriented between catalyst layers 104, 106.
  • PEM Proton Exchange Membrane
  • the catalyst layers and membrane define a membrane electrode assembly 108.
  • the membrane electrode assembly is positioned between opposing substrates 110, 112 that function as gas diffusion layers.
  • anode structure 111 Adjacent to substrate 110 and opposing the membrane electrode assembly is an anode structure 111 that includes an array 113 of ribs (e.g., ribs 114, 116).
  • Channels of array 113 e.g., channel 118
  • each channel of array 113 is defined by a pair of adjacent ribs, a corresponding channel wall of the anode, and a corresponding portion of substrate 110.
  • channel 118 is defined by ribs 114 and 116, channel wall 120, and a portion 122 of substrate 110.
  • the channels of array 113 are reactant channels, with the reactant or fuel of this embodiment being a hydrogen-rich gas (e.g., hydrogen gas).
  • a cathode structure 121 Adjacent to substrate 112 and opposing the membrane electrode assembly is a cathode structure 121 that includes an array 123 of ribs (e.g., ribs 124, 126). Channels of array 123 (e.g., channel 128) that form a flow field are defined between the ribs.
  • each channel of array 123 is defined by a pair of adjacent ribs, a corresponding channel wall of the cathode, and a corresponding portion of substrate 112.
  • channel 128 is defined by ribs 124 and 126, channel wall 130, and a portion 132 of substrate 112.
  • the channels of array 123 are reactant channels, with the reactant or oxidant being an oxygen-rich gas (e.g., air).
  • the reactant or oxidant being an oxygen-rich gas (e.g., air).
  • water can be present in any of the reactant channels.
  • the flow field of reactant channels of fuel cell system 100 is shown in greater detail in FIG. 2. As shown in FIG. 2, the channels extend from open ends located along a first side 140 of the flow field to open ends located along an opposing second side 142 of the flow field.
  • channel 108 extends between open ends 144 and 146, and channel 148 extends between open ends 154, 156.
  • the channels are straight channels in this embodiment, various other configurations can be used, including those in which the open ends of a channel are not located along opposing sides of the fuel cell.
  • Fuel cell system 100 also includes two fluid manifold assemblies.
  • a first manifold assembly 160 (which incorporates manifolds 162 and 164) is positioned along side 140 of the flow field, and a second manifold assembly 165 is positioned along side 142.
  • a first set 166 of the channels (which includes channel 108) extends between and communicates with manifold 162 and manifold assembly 165.
  • a second set 168 of the channels (which includes channel 148) extends between and communicates with manifold 164 and manifold assembly 165.
  • the flow field In operation in a high power mode, the flow field is operated so that fluid (e.g., air) enters each of the channels at side 140 of the fuel cell and departs the channels at side 142, thereby providing a single-pass configuration.
  • fluid e.g., air
  • the flow field is operated so that fluid is evenly distributed among all of the channels and effectively flows over the distance of the length of the channels.
  • Such a single-pass configuration is considered adequate for reducing a tendency for water to hang-up in the channels since the high power operation uses relatively high fluid flow velocities through the flow field.
  • This configuration also exhibits a relatively low pressure drop across the flow field.
  • the flow field can be dynamically altered (via the manifold assemblies in this embodiment) to exhibit a multi-pass configuration.
  • manifold assembly 165 is altered so that fluid is redirected to flow through the second set of channels 168 and the manifold 164. That is, fluid, which directed through manifold 162 and the first set of channels 166 to manifold assembly 165, is also directed through the second set of channels 168 and manifold 164. Effectively, the cross-sectional area through which the fluid flows is reduced and the distance along which the fluid flows is increased.
  • This multi-pass configuration increases the fluid flow velocity through the channels (e.g., to a velocity comparable to that exhibited during the high power mode) and tends to assist in clearing the channels of hang-ups. It should be noted that although the embodiment of FIGS. 1 - 3 is configured to be selectively alterable between a multi-pass configuration (using only two passes) and a single-pass configuration, other numbers of passes can be used in other embodiments.
  • fuel cell system 200 incorporates a flow field 202 of channels (e.g., channels 204 and 206). Each of the channels extends from an open end located along a first side 208 of the flow field to an open end located along an opposing second side 210.
  • channel 204 extends between open ends 214 and 216
  • channel 222 extends between open ends 224 and 226.
  • Fuel cell system 200 also includes two fluid manifold assemblies. In particular, a first manifold assembly 230 is positioned along side 208 of the flow field and a second manifold assembly 240 is positioned along side 210.
  • Manifold assembly 230 incorporates manifolds 232, 234 and a valve 236.
  • manifold assembly 240 incorporates manifolds 242, 244 and a valve 246.
  • a first set 248 of the channels (which includes channel 204) extends between and communicates with manifold assemblies 230 and 240. Specifically, each of the channels of set 248 extends between manifolds 232 and 242.
  • a second set 250 of the channels (which includes channel 206) also extends between and communicates with manifold assemblies 230 and 240. Specifically, each of the channels of set 250 extends between manifolds 234 and 244.
  • flow field 202 is operated so that fluid (e.g., air) enters each of the channels via manifold assembly 230 and departs the channels via manifold assembly 240.
  • fluid e.g., air
  • Such a single-pass configuration is considered adequate for reducing a tendency for water to hang-up in the channels since the high power operation uses relatively high fluid flow velocities.
  • the single-pass configuration of this embodiment is facilitated by moving valves 236 and 246 to respective first positions. Specifically, in the first position, valve 236 is configured so that fluid flow directed to valve 236 is routed to manifold 234. As such, fluid is first routed to the open ends of the channels of the flow field that communicate with manifold assembly 230.
  • Valve 246 in the first position is configured to route fluid provided via manifold assembly 240 away from the flow field.
  • operation in a low power mode typically involves lower fluid flow velocities that might result in water hang-up if the flow field were operated in the single- pass configuration.
  • the flow field can be dynamically altered to exhibit a multi-pass configuration.
  • the multi-pass configuration of this embodiment is facilitated by moving valves 236 and 246 to respective second positions.
  • valve 246 is moved to the second position in which valve 246 is configured to direct fluid from the first set of channels (and manifold 242) to (manifold 244 and) set 250 of the channels.
  • valve 236 is configured to receive fluid provided by manifold 234 and set 250 of the channels.

Landscapes

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

Abstract

Fuel cell systems (200) and methods involving variable numbers of flow field passes are provided. In this regard, a representative method for operating a fuel cell includes: operating a flow field (202) of a fuel cell with a first number of passes; and dynamically altering the flow field such that the flow field uses a different number of passes.

Description

FUEL CELL SYSTEMS AND METHODS INVOLVING VARIABLE NUMBERS OF FLOW FIELD PASSES
BACKGROUND Technical Field
The disclosure generally relates to fuel cells.
Description of the Related Art
Some fuel cell systems are designed to operate at both high power and low power ranges. In this regard, flow fields of fuel cell systems optimized for high power operation tend to exhibit instability during low power operation. This may be caused due to lower fluid flow velocities and consequent water hang-up within channels of the flow fields, for example. With respect to fuel cell systems designed for low power operation, high power operation tends to result in increased parasitic loads and system complexity.
SUMMARY
Fuel cell systems and methods involving variable numbers of flow field passes are provided. In this regard, an exemplary embodiment of a fuel cell system comprises: a fuel cell flow field having sets of channels operative to route fluid; the flow field being operative such that, in a first mode, fluid is routed through the sets of channels in a first number of passes and, in a second mode, fluid is routed through the sets of channels in a different number of passes. An exemplary embodiment of a fuel cell comprises: a flow field having a first set of channels, a second set of channels, a first manifold assembly and a second manifold assembly, the first set of channels extending between and communicating with the first manifold assembly and the second manifold assembly, the second set of channels extending between and communicating with the first manifold assembly and the second manifold assembly; the flow field being operative such that, in a first mode, fluid is routed from the first manifold assembly to the first set of channels and the second set of channels and, in a second mode, fluid is routed from the first manifold assembly to the first set of channels, through the second manifold assembly, and thereafter to the second set of channels.
An exemplary embodiment of a method for operating a fuel cell comprises: operating a flow field of a fuel cell with a first number of passes; and dynamically altering the flow field such that the flow field uses a different number of passes.
Other systems, methods, features and/or advantages of this disclosure will be or may become apparent to one with skill in the art upon examination of the following drawings and detailed description. It is intended that all such additional systems, methods, features and/or advantages be included within this description and be within the scope of the present disclosure.
BRIEF DESCRIPTION OF THE DRAWINGS
Many aspects of the disclosure can be better understood with reference to the following drawings. The components in the drawings are not necessarily to scale. Moreover, in the drawings, like reference numerals designate corresponding parts throughout the several views.
FIG. 1 is a schematic diagram partially depicting an exemplary embodiment of a fuel cell system.
FIG. 2 is a schematic diagram depicting the fuel cell system of FIG. 1 , showing detail of the flow field.
FIG. 3 is a schematic diagram of the embodiment of FIG. 1 being operated at a low power level.
FIG. 4 is the schematic diagram depicting another embodiment of a fuel cell system being operated at a low power level.
FIG. 5 is a schematic diagram depicting the embodiment of FIG. 4 being operated at a high power level.
DETAILED DESCRIPTION
Fuel cell systems and methods involving variable numbers of passes are provided. In this regard, several embodiments incorporate the use of manifold assemblies that can be dynamically altered to vary the number of passes through a flow field. By way of example, for low power operations, one or more valves can be selectively positioned such that a multi-pass configuration is provided. For high power operations, the valves can be repositioned to operate the flow field with fewer passes. For instance, the flow field can be operated as a single-pass flow field.
An exemplary embodiment of a fuel cell system is partially depicted in the schematic diagram of FIG. 1. As shown in FIG. 1 , fuel cell system 100 is configured as a Proton Exchange Membrane (PEM) fuel cell incorporating a membrane 102 that is oriented between catalyst layers 104, 106. The catalyst layers and membrane define a membrane electrode assembly 108. The membrane electrode assembly is positioned between opposing substrates 110, 112 that function as gas diffusion layers.
Adjacent to substrate 110 and opposing the membrane electrode assembly is an anode structure 111 that includes an array 113 of ribs (e.g., ribs 114, 116). Channels of array 113 (e.g., channel 118) that form a flow field are defined between the ribs. In particular, each channel of array 113 is defined by a pair of adjacent ribs, a corresponding channel wall of the anode, and a corresponding portion of substrate 110. By way of example, channel 118 is defined by ribs 114 and 116, channel wall 120, and a portion 122 of substrate 110. Notably, the channels of array 113 are reactant channels, with the reactant or fuel of this embodiment being a hydrogen-rich gas (e.g., hydrogen gas).
Adjacent to substrate 112 and opposing the membrane electrode assembly is a cathode structure 121 that includes an array 123 of ribs (e.g., ribs 124, 126). Channels of array 123 (e.g., channel 128) that form a flow field are defined between the ribs. In particular, each channel of array 123 is defined by a pair of adjacent ribs, a corresponding channel wall of the cathode, and a corresponding portion of substrate 112. By way of example, channel 128 is defined by ribs 124 and 126, channel wall 130, and a portion 132 of substrate 112. In this embodiment, the channels of array 123 are reactant channels, with the reactant or oxidant being an oxygen-rich gas (e.g., air). Notably, during operation, water can be present in any of the reactant channels. The flow field of reactant channels of fuel cell system 100 is shown in greater detail in FIG. 2. As shown in FIG. 2, the channels extend from open ends located along a first side 140 of the flow field to open ends located along an opposing second side 142 of the flow field. By way of example, channel 108 extends between open ends 144 and 146, and channel 148 extends between open ends 154, 156. Although the channels are straight channels in this embodiment, various other configurations can be used, including those in which the open ends of a channel are not located along opposing sides of the fuel cell.
Fuel cell system 100 also includes two fluid manifold assemblies. In particular, a first manifold assembly 160 (which incorporates manifolds 162 and 164) is positioned along side 140 of the flow field, and a second manifold assembly 165 is positioned along side 142. Notably, a first set 166 of the channels (which includes channel 108) extends between and communicates with manifold 162 and manifold assembly 165. A second set 168 of the channels (which includes channel 148) extends between and communicates with manifold 164 and manifold assembly 165.
In operation in a high power mode, the flow field is operated so that fluid (e.g., air) enters each of the channels at side 140 of the fuel cell and departs the channels at side 142, thereby providing a single-pass configuration. Thus, the flow field is operated so that fluid is evenly distributed among all of the channels and effectively flows over the distance of the length of the channels. Such a single-pass configuration is considered adequate for reducing a tendency for water to hang-up in the channels since the high power operation uses relatively high fluid flow velocities through the flow field. This configuration also exhibits a relatively low pressure drop across the flow field. In contrast, operation in a low power mode typically involves lower fluid flow velocities through the flow field that might result in water hang-up if the flow field were operated in the single-pass configuration. In order to reduce the potential for water hang-up, the flow field can be dynamically altered (via the manifold assemblies in this embodiment) to exhibit a multi-pass configuration. Specifically, as shown in FIG. 3, manifold assembly 165 is altered so that fluid is redirected to flow through the second set of channels 168 and the manifold 164. That is, fluid, which directed through manifold 162 and the first set of channels 166 to manifold assembly 165, is also directed through the second set of channels 168 and manifold 164. Effectively, the cross-sectional area through which the fluid flows is reduced and the distance along which the fluid flows is increased.
This multi-pass configuration increases the fluid flow velocity through the channels (e.g., to a velocity comparable to that exhibited during the high power mode) and tends to assist in clearing the channels of hang-ups. It should be noted that although the embodiment of FIGS. 1 - 3 is configured to be selectively alterable between a multi-pass configuration (using only two passes) and a single-pass configuration, other numbers of passes can be used in other embodiments.
A portion of another embodiment of a fuel cell system is depicted schematically in FIG. 4. As shown in FIG. 4, fuel cell system 200 incorporates a flow field 202 of channels (e.g., channels 204 and 206). Each of the channels extends from an open end located along a first side 208 of the flow field to an open end located along an opposing second side 210. By way of example, channel 204 extends between open ends 214 and 216, and channel 222 extends between open ends 224 and 226. Fuel cell system 200 also includes two fluid manifold assemblies. In particular, a first manifold assembly 230 is positioned along side 208 of the flow field and a second manifold assembly 240 is positioned along side 210. Manifold assembly 230 incorporates manifolds 232, 234 and a valve 236. Similarly, manifold assembly 240 incorporates manifolds 242, 244 and a valve 246.
A first set 248 of the channels (which includes channel 204) extends between and communicates with manifold assemblies 230 and 240. Specifically, each of the channels of set 248 extends between manifolds 232 and 242. A second set 250 of the channels (which includes channel 206) also extends between and communicates with manifold assemblies 230 and 240. Specifically, each of the channels of set 250 extends between manifolds 234 and 244.
In operation in a high power mode (FIG. 5), flow field 202 is operated so that fluid (e.g., air) enters each of the channels via manifold assembly 230 and departs the channels via manifold assembly 240. Such a single-pass configuration is considered adequate for reducing a tendency for water to hang-up in the channels since the high power operation uses relatively high fluid flow velocities. Notably, the single-pass configuration of this embodiment is facilitated by moving valves 236 and 246 to respective first positions. Specifically, in the first position, valve 236 is configured so that fluid flow directed to valve 236 is routed to manifold 234. As such, fluid is first routed to the open ends of the channels of the flow field that communicate with manifold assembly 230. Valve 246 in the first position is configured to route fluid provided via manifold assembly 240 away from the flow field. In contrast, operation in a low power mode typically involves lower fluid flow velocities that might result in water hang-up if the flow field were operated in the single- pass configuration. In order to reduce the potential for water hang-up, the flow field can be dynamically altered to exhibit a multi-pass configuration. Specifically, as shown in FIG. 4, the multi-pass configuration of this embodiment is facilitated by moving valves 236 and 246 to respective second positions. In particular, valve 246 is moved to the second position in which valve 246 is configured to direct fluid from the first set of channels (and manifold 242) to (manifold 244 and) set 250 of the channels. Thus, the effective number of channels is reduced and the distance along which the fluid flows is increased. This configuration increases the fluid flow velocity through the channels (e.g., to a velocity comparable to that exhibited during the high power mode for flow rates that are proportional to the low power mode) and tends to assist in clearing the channels of hang-ups. Additionally, in the second position, valve 236 is configured to receive fluid provided by manifold 234 and set 250 of the channels.
It should be emphasized that the above-described embodiments are merely possible examples of implementations set forth for a clear understanding of the principles of this disclosure. Many variations and modifications may be made to the above-described embodiments without departing substantially from the spirit and principles of the disclosure. All such modifications and variations are intended to be included herein within the scope of this disclosure and protected by the accompanying claims.

Claims

1. A fuel cell system comprising: a fuel cell flow field having sets of channels operative to route fluid; the flow field being operative such that, in a first mode, fluid is routed through the sets of channels in a first number of passes and, in a second mode, fluid is routed through the sets of channels in a different number of passes.
2. The system of claim 1 , wherein, in the first mode, the flow field is operated as a single-pass flow field.
3. The system of claim 1 , wherein: the sets of channels include a first set of channels and a second set of channels; the system further comprises a first valve movable between a first position corresponding to the first mode, in which fluid is routed to both the first set of channels and the second set of channels, and a second position corresponding to the second mode, in which fluid is not routed to the second set of channels.
4. The system of claim 3, further comprising a second valve movable between a first position corresponding to the first mode, in which fluid from both the first set of channels and the second set of channels is received at the second valve, and a second position corresponding to the second mode, in which fluid passed through the first set of channels is routed via the second valve to the second set of channels.
5. The system of claim 1 , wherein the flow field is a Proton Exchange Membrane (PEM) fuel cell flow field.
6. The system of claim 1 , wherein the sets of channels are reactant channels.
7. The system of claim 6, wherein the fluid used as a reactant is air.
8. A fuel cell comprising: a flow field having a first set of channels, a second set of channels, a first manifold assembly and a second manifold assembly, the first set of channels extending between and communicating with the first manifold assembly and the second manifold assembly, the second set of channels extending between and communicating with the first manifold assembly and the second manifold assembly; the flow field being operative such that, in a first mode, fluid is routed from the first manifold assembly to the first set of channels and the second set of channels and, in a second mode, fluid is routed from the first manifold assembly to the first set of channels, through the second manifold assembly, and thereafter to the second set of channels.
9. The fuel cell of claim 8, wherein: the first manifold assembly comprises a first manifold and a second manifold; the first set of channels communicates with the first manifold; and the second set of channels communicates with the second manifold.
10. The fuel cell of claim 9, wherein: the fuel cell further comprises a valve; in the first mode, the valve is operative to route fluid to the second manifold; and in the second mode, the valve is operative to prevent fluid from being routed to the second manifold.
11. The fuel cell of claim 8, wherein: the second manifold assembly comprises a first manifold and a second manifold; the first set of channels communicates with the first manifold; and the second set of channels communicates with the second manifold.
12. The fuel cell of claim 11 , wherein: the fuel cell further comprises a valve; in the first mode, the valve is operative to receive fluid from both the first manifold and the second manifold; and in the second mode, the valve is operative to route fluid from the first manifold to the second manifold.
13. The fuel cell of claim 8, wherein the fuel cell is a Proton Exchange Membrane (PEM) fuel cell.
14. A method for operating a fuel cell comprising: operating a flow field of a fuel cell with a first number of passes; and dynamically altering the flow field such that the flow field uses a different number of passes.
15. The method of claim 14, wherein the different number is a higher number of passes than the first number.
16. The method of claim 15, wherein the first number is one and the different number is two.
17. The method of claim 15, wherein the different number is a lower number of passes than the first number.
18. The method of claim 14, wherein the flow field is a Proton Exchange Membrane (PEM) fuel cell flow field.
19. The method of claim 14, wherein the flow field comprises reactant channels.
20. The method of claim 19, wherein the fluid used as a reactant is air.
PCT/US2007/087882 2007-12-18 2007-12-18 Fuel cell systems and methods involving variable numbers of flow field passes WO2009078866A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/US2007/087882 WO2009078866A1 (en) 2007-12-18 2007-12-18 Fuel cell systems and methods involving variable numbers of flow field passes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US2007/087882 WO2009078866A1 (en) 2007-12-18 2007-12-18 Fuel cell systems and methods involving variable numbers of flow field passes

Publications (1)

Publication Number Publication Date
WO2009078866A1 true WO2009078866A1 (en) 2009-06-25

Family

ID=39387259

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2007/087882 WO2009078866A1 (en) 2007-12-18 2007-12-18 Fuel cell systems and methods involving variable numbers of flow field passes

Country Status (1)

Country Link
WO (1) WO2009078866A1 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0159438A2 (en) * 1984-03-27 1985-10-30 Kyushu University Multi-layered thin film heat transfer gauge
JP2003100320A (en) * 2001-09-20 2003-04-04 Toyota Motor Corp Fuel cell
US20040091760A1 (en) * 2002-07-04 2004-05-13 Shunsuke Mizutani Fuel cell
EP1450432A2 (en) * 2003-02-20 2004-08-25 Matsushita Electric Industrial Co., Ltd. Polymer electrolyte fuel cell
WO2005121917A1 (en) * 2004-06-10 2005-12-22 National Research Council Of Canada Flow control apparatus and method for fuel cell flow fields

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0159438A2 (en) * 1984-03-27 1985-10-30 Kyushu University Multi-layered thin film heat transfer gauge
JP2003100320A (en) * 2001-09-20 2003-04-04 Toyota Motor Corp Fuel cell
US20040091760A1 (en) * 2002-07-04 2004-05-13 Shunsuke Mizutani Fuel cell
EP1450432A2 (en) * 2003-02-20 2004-08-25 Matsushita Electric Industrial Co., Ltd. Polymer electrolyte fuel cell
WO2005121917A1 (en) * 2004-06-10 2005-12-22 National Research Council Of Canada Flow control apparatus and method for fuel cell flow fields

Similar Documents

Publication Publication Date Title
JP4598287B2 (en) FUEL CELL STACK AND METHOD OF OPERATING FUEL CELL STACK
JP5962847B2 (en) FUEL CELL, FUEL CELL DISTRIBUTION DEVICE, AND VEHICLE HAVING FUEL CELL
JP2008226838A (en) Two-way branch of channel in flow field of dipole plate
US7781119B2 (en) Flow shifting in each individual cell of a fuel cell stack
WO2005122305A1 (en) Fuel cell stack with even distributing gas manifolds
CA2549668A1 (en) Fuel cell and separator for fuel cell
US10090535B2 (en) Fuel cell having at least one active surface layer
JP2006351222A (en) Separator for fuel cell and fuel cell
US20070254203A1 (en) Fuel cell stack
US11038181B2 (en) Fuel cells with a non-parallel gas flow channel configuration and methods thereof
US8101313B2 (en) Flow field plate module for fuel cell system
WO2006062242A1 (en) Improvement of flow distribution characteristics of fuel cell
JP5112004B2 (en) Fuel cell
US20230361318A1 (en) Bipolar plate
JP5082313B2 (en) Fuel cell separator structure
KR102579354B1 (en) Separator for feul cell
JP5274908B2 (en) Fuel cell stack
WO2009078866A1 (en) Fuel cell systems and methods involving variable numbers of flow field passes
JP5216391B2 (en) Fuel cell separator
CN107834086A (en) Fuel battery double plates
JP2006221896A (en) Fuel cell and separator for fuel cell
JP5123824B2 (en) FUEL CELL STACK AND METHOD OF OPERATING FUEL CELL STACK
US8318371B2 (en) Separator for fuel cell and fuel cell stack using the same
JP5144388B2 (en) Fuel cell stack
JP2008171587A (en) Fuel cell system

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 07865791

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 07865791

Country of ref document: EP

Kind code of ref document: A1