GB2372144A - Fuel cell stack incorporating integral flow field plates and gas diffusion layer - Google Patents
Fuel cell stack incorporating integral flow field plates and gas diffusion layer Download PDFInfo
- Publication number
- GB2372144A GB2372144A GB0103391A GB0103391A GB2372144A GB 2372144 A GB2372144 A GB 2372144A GB 0103391 A GB0103391 A GB 0103391A GB 0103391 A GB0103391 A GB 0103391A GB 2372144 A GB2372144 A GB 2372144A
- Authority
- GB
- United Kingdom
- Prior art keywords
- channels
- fuel cell
- gas diffusion
- cell stack
- flow field
- 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.)
- Granted
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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
- H01M8/026—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant characterised by grooves, e.g. their pitch or depth
-
- 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
- H01M8/02—Details
- H01M8/0202—Collectors; Separators, e.g. bipolar separators; Interconnectors
- H01M8/0258—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant
- H01M8/0265—Collectors; Separators, e.g. bipolar separators; Interconnectors characterised by the configuration of channels, e.g. by the flow field of the reactant or coolant the reactant or coolant channels having varying cross sections
-
- 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
- H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
-
- 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
Abstract
A fuel cell stack comprises a plurality of flow field plates having on at least one face an assembly of channels comprising one or more gas delivery channels 3, 4 and a plurality of gas diffusion channels 2 of width less than 0.2mm connecting thereto, the gas diffusion channels acting as a gas diffusion layer integral with the flow field plate.
Description
FUEL CELL STACK INCORPORATING INTEGRAL FLOW FIELD PLATES AND GAS DIFFUSION LAYER This invention relates to fuel cells and is particularly, although not exclusively, applicable to proton exchange membrane fuel cells.
Fuel cells are devices in which a fuel and an oxidant combine in a controlled manner to produce electricity directly. By directly producing electricity without intermediate combustion and generation steps, the electrical efficiency of a fuel cell is higher than using the fuel in a traditional generator. This much is widely known. A fuel cell sounds simple and desirable but many man-years of work have been expended in recent years attempting to produce practical fuel cell systems.
One type of fuel cell in commercial production is the so-called proton exchange membrane (PEM) fuel cell sometimes called polymer electrolyte or solid polymer fuel cells (PEFCs)].
Such cells use hydrogen as a fuel and comprise an electrically insulating (but ionically conducting) polymer membrane having porous electrodes disposed on both faces. The membrane is typically a fluorosulphonate polymer and the electrodes typically comprise a noble metal catalyst dispersed on a carbonaceous powder substrate. This assembly of electrodes and membrane is often referred to as the membrane electrode assembly (MEA).
Hydrogen fuel is supplied to one electrode (the anode) where it is oxidised to release electrons to the anode and hydrogen ions to the electrolyte. Oxidant (typically air or oxygen) is supplied to the other electrode (the cathode) where electrons from the cathode combine with the oxygen and the hydrogen ions to produce water.
In commercial PEM fuel cells many such membranes are stacked together separated by flow field plates (also referred to as bipolar plates). The flow field plates are typically formed of metal or graphite to permit good transfer of electrons between the anode of one membrane and the cathode of the adjacent membrane. The flow field plates have a pattern of grooves on their surface to supply fluid (fuel or oxidant) and to remove water produced as a reaction product of the fuel cell. Various methods of producing the grooves have been described, for example it has been proposed to form such grooves by machining, embossing or moulding (WOOO/41260), and (as is particularly useful for the present invention) by sandblasting through a resist (WOO 1/04982).
To ensure that the fluids are dispersed evenly to their respective electrode surfaces a so-called gas diffusion layer (GDL) is placed between the electrode and the flow field plate. The gas diffusion layer is a porous material and typically comprises a carbon paper or cloth, often having a bonded layer of carbon powder on one face and coated with a hydrophobic material to promote water rejection. It has been proposed to provide an interdigitated flow field below a macroporous material (US-A-5641586) having connected porosity of pore size range 20 1OOum allowing a reduction in size of the gas diffusion layer. Such an arrangement permits gas flow around blocked pores, which is disadvantageous. Build up of reactant products (such as water) can occur in these pores reducing gas transport efficiency. Additionally, such a structure increases the thickness of the flow field plate.
A combined flow field plate and gas diffusion layer has been described in US-A-6037073 and comprises a selectively impregnated body of porous carbon material, the impregnation hermetically sealing part of the plate. Such an arrangement has the drawbacks that it is complicated to make reproducibly and that it permits gas flow around blockages as in
US-A-5641586.
An assembled body of flow field plates and membranes with associated fuel and oxidant supply manifolds is often referred to a fuel cell stack.
Although the technology described above has proved useful in prototype and in some limited commercial applications, to achieve wider commercial acceptance there is now a demand to reduce the physical size of a fuel cell stack and to reduce its cost. Accordingly, a reduction in the number of components could have beneficial results on size and cost (both through material and assembly costs). Also, the prior art flow field plates have provided flow fields of serpentine, linear, or interdigitated form but have not looked to other physical systems for improving the gas flow pathways.
The applicants have realised that by forming sufficiently fine channels on the face of the flow field plates the purpose of distributing the gas evenly across the electrodes can be achieved without the use of a separate gas diffusion layer. They have further realised that by looking to physiological systems (the lung) improved flow field geometries may be realised that are likely to have lower parasitic losses due to their shorter gas flow pathways.
The present invention therefore provides a fuel cell stack comprising a plurality of flow field plates having on at least one face an assembly of channels comprising one or more gas delivery channels and a plurality of gas diffusion channels of width less than 0. 2mm connecting thereto, the gas diffusion channels acting as a gas diffusion layer integral with the flow field plate.
The gas delivery channels may comprise one or more primary channels of a width greater than 1mm, and a plurality of secondary gas delivery channels of a width less than lmm connecting thereto.
The gas diffusion channels may form a branched structure.
The gas diffusion channels may be of varying width, forming a branched structure of progressively diminishing channel width similar to the branching structure of blood vessels and air channels in the lung.
The invention is illustrated by way of non-limitative example in the following description with reference to the drawing in which :
Fig. 1 shows schematically in part section a part of a fluid flow plate incorporating gas delivery channels and gas diffusion channels formed by sandblasting.
Fig. 2 shows schematically a partial plan view of a fluid flow plate incorporating gas delivery channels and gas diffusion channels.
To form both gas delivery and gas diffusion channels a technique such as sand blasting may be used in which a template or resist is placed against the surface of a plate, the template or resist having a pattern corresponding to the desired channel geometry. Such a technique is described in WO01/04982, which is incorporated herein in its entirety as enabling the present invention. With this technique the plates may be formed from a graphite/resin composite or other non-porous electrically conductive material that does not react significantly with the reactants used.
It is found with this technique that the profiles of channels of different width vary due to the shadow cast by the mask. Fig. 1 shows a flow field plate I having a narrow channel 2 formed in its surface. Because of the shadowing effect of the resist used in forming the channel the channel is exposed to sandblast grit coming effectively only from directly above. This leads to a generally semicircular profile to the channel and to a shallow cutting of the channel.
For progressively larger channels (3 and 4) the resist casts less of a shadow allowing sandblasting grit from a progressively wider range of angles to strike the surface of the flow field plate, so allowing both deeper cutting of the surface and a progressively flatter bottom to the channel.
Accordingly, by applying a resist with different width channels to a plate and exposing the plate and resist to sandblasting with a fine grit, a pattern of channels of different widths and depths can be applied.
Applying such a pattern of channels of varying width and depth has advantages. In flow field plates the purpose behind the channels conventionally applied is to try to ensure a uniform supply of reactant material to the electrodes and to ensure prompt removal of reacted products. However the length of the passage material has to travel is high since a convoluted path is generally used.
Another system in which the aim is to supply reactant uniformly to a reactant surface and to remove reacted products is the lung. In the lung an arrangement of progressively finer channels is provided so that air has a short pathway to its reactant site in the lung, and carbon dioxide has a short pathway out again. By providing a network of progressively finer channels into the flow field plate, reactant gases have a short pathway to their reactant sites.
The finest channels could simply discharge into wide gas removal channels or, as in the lung, a corresponding network of progressively wider channels could be provided out of the flow field plate. In the latter case, the two networks of progressively finer channels and progressively wider channels could be connected end-to-end or arranged as interdigitated networks, with diffusion through the electrode material providing connectivity. Connection end-to-end provides the advantage that a high pressure will be maintained through the channels, assisting in the removal of blockages.
The question of interconnected channels vs. blind channels depends on which side of the electrode we are dealing with. Hydrogen ions travel from the anode, through the polymer, and are made into water at the cathode. All of the water is made on the cathode or oxygen side of the cell. The water generation on the cathode side means that the air side gas channels cannot be blind ended, as this would cause flooding. Interdigitated will also be tricky unless a
GDL is used as the permeability of the electrode is not high. Accordingly, the model wherein the branched channels join end to end or drain to a larger channel is preferred.
Fig. 2 shows in a schematic plan a portion of a flow field plate having broad primary gas delivery channels 4, which diverge into secondary gas delivery channels 3 which themselves diverge into gas diffusion channels 2. Gas diffusion channels 5 can also come off the primary gas deliver channels 4 if required. The primary and secondary gas delivery channels may each form a network of progressively finer channels as may the gas diffusion channels and the arrangement of the channels may resemble a fractal arrangement.
The primary gas delivery channels may have a width of greater than lmm, for example about 2mm. A typical depth of such a channel is 0.25mm but depth is limited only by the need to have sufficient strength in the flow field plate after forming the channel. The secondary gas delivery channels may have a width of less than lmm, for example 0. 5mm and will be shallower than the primary gas delivery channels. The gas diffusion channels have a width of less than 0.2mm, for example about 1OOu. m and will be shallower still.
By providing such a structure, reactant products have a short distance to travel and can be removed efficiently in comparison with conventional plate designs. Additionally, gas channels in typical bipolar plates are of square or rectangular section and are millimetric in size. E. g. BallardTM plates have a 2.5mm square section channel. APSTM plates have a channel that is 0. 9mm wide by 0.6 mm deep. Smaller channels are beneficial as the pressure drop per unit length is higher and the pressure drop is what drives the reactants into the diffusion media.
WOOO/41260 has an extensive discussion of flow field design but has not appreciated that be providing extremely fine channels (less than 0. 2mm) and by providing such channels as part of a network of progressively diminishing width, the pressure drop between adjacent channels is minimised so avoiding short-circuiting of the flow field.
The primary channel (s) must be of a size sufficient to deliver the working volume of gas required by the cell. This is about 25L/min per kW of working power.
The gas diffusion channels are provided in a sufficient density over the surface of the flow field plate to provide sufficient gas delivery that a gas diffusion layer may be omitted.
The limit on channel width is a function of the mask thickness used in the sand blast process.
Image Pro materials (Chromaline Corp. US), are very thick at 125 micron. These masks limit track width to about 100 microns. Other mask materials can be spray coated onto the substrate and exposed in situ. These materials are much more resilient and hence can be much thinner. Chromaline SBXTM can be used to etch features down to 10-20 microns wide.
As well known, (see for example WOOO/41260) the same pattern of grooves does not need to be applied to both faces of a flow field plate and the present invention is not limited in this way.
Claims (7)
1. A fuel cell stack comprising a plurality of flow field plates having on at least one face an assembly of channels comprising one or more gas delivery channels and a plurality of gas diffusion channels of width less than 0. 2mm connecting thereto, the gas diffusion channels acting as a gas diffusion layer integral with the flow field plate.
2. A fuel cell stack as claimed in Claim 1, in which the gas delivery channels comprise one or more primary channels of a width greater than lmm, and a plurality of secondary gas delivery channels of a width less than lmm connecting thereto
3. A fuel cell stack as claimed in Claim 1 or Claim 2, in which the gas diffusion channels form a branched structure.
4. A fuel cell stack as claimed in Claim 3 in which the gas diffusion channels are of varying width forming a branched structure of progressively diminishing channel width.
5. A fuel cell stack as claimed in any preceding claim comprising a first assembly of channels for gas delivery and a second assembly of channels for removal of reactant products.
6. A fuel cell stack as claimed in claim 5, in which the first and second assemblies of channels are interdigitated.
7. A fuel cell stack as claimed in any preceding claim in which channels decrease in depth with diminishing width.
Priority Applications (19)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0103391A GB2372144B (en) | 2001-02-12 | 2001-02-12 | Fuel cell stack incorporating integral flow field plates and gas diffusion layer |
EP02710180A EP1264360B1 (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
CA002437891A CA2437891A1 (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
US10/380,356 US7067213B2 (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
CA2437892A CA2437892C (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
DE60212001T DE60212001T2 (en) | 2001-02-12 | 2002-02-05 | FLUID DISTRIBUTION PLATE GEOMETRIES |
MXPA03007132A MXPA03007132A (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries. |
PCT/GB2002/000479 WO2002065565A2 (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
TW091101980A TW569486B (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
KR1020037010515A KR100840585B1 (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
KR10-2003-7010514A KR20030081438A (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
CNB028048695A CN100459254C (en) | 2001-02-12 | 2002-02-05 | Flow field plate Geometries |
PCT/GB2002/000491 WO2002065566A1 (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
MXPA03007131A MXPA03007131A (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries. |
JP2002564777A JP4291575B2 (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometry |
EP02710172A EP1405359A2 (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
JP2002564776A JP2004523069A (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometry |
CNA028048687A CN1491446A (en) | 2001-02-12 | 2002-02-05 | Flow field plate geometries |
AT02710180T ATE329375T1 (en) | 2001-02-12 | 2002-02-05 | FLUID DISTRIBUTION PLATE GEOMETRIES |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB0103391A GB2372144B (en) | 2001-02-12 | 2001-02-12 | Fuel cell stack incorporating integral flow field plates and gas diffusion layer |
Publications (3)
Publication Number | Publication Date |
---|---|
GB0103391D0 GB0103391D0 (en) | 2001-03-28 |
GB2372144A true GB2372144A (en) | 2002-08-14 |
GB2372144B GB2372144B (en) | 2003-02-12 |
Family
ID=9908542
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB0103391A Expired - Fee Related GB2372144B (en) | 2001-02-12 | 2001-02-12 | Fuel cell stack incorporating integral flow field plates and gas diffusion layer |
Country Status (1)
Country | Link |
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GB (1) | GB2372144B (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2403061A (en) * | 2003-06-18 | 2004-12-22 | Morgan Crucible Co | Flow field plate geometries |
US7067213B2 (en) | 2001-02-12 | 2006-06-27 | The Morgan Crucible Company Plc | Flow field plate geometries |
US7838139B2 (en) | 2002-06-24 | 2010-11-23 | The Morgan Crucible Company Plc | Flow field plate geometries |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001004982A1 (en) * | 1999-07-08 | 2001-01-18 | Loughborough University Innovations Limited | Flow field plates |
-
2001
- 2001-02-12 GB GB0103391A patent/GB2372144B/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2001004982A1 (en) * | 1999-07-08 | 2001-01-18 | Loughborough University Innovations Limited | Flow field plates |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7067213B2 (en) | 2001-02-12 | 2006-06-27 | The Morgan Crucible Company Plc | Flow field plate geometries |
US7838139B2 (en) | 2002-06-24 | 2010-11-23 | The Morgan Crucible Company Plc | Flow field plate geometries |
GB2403061A (en) * | 2003-06-18 | 2004-12-22 | Morgan Crucible Co | Flow field plate geometries |
GB2403061B (en) * | 2003-06-18 | 2005-05-11 | Morgan Crucible Co | Flow field plate geometries |
Also Published As
Publication number | Publication date |
---|---|
GB2372144B (en) | 2003-02-12 |
GB0103391D0 (en) | 2001-03-28 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |
Effective date: 20050212 |