FLUID FLOW PLATE FOR A FUEL CELL
The invention relates to fluid flow plates for electrochemical fuel cell assemblies, and in
particular to configurations of bipolar or monopolar plates allowing for multiple fluid flow
channels for the passage of two or more of anode, cathode and coolant fluids.
The use of bipolar, as opposed to unipolar, plates in electrochemical fuel cells allows for a
reduction in thickness and consequently overall size of the fuel cell, due to the use of
shared electrical connections between the anode plate of one cell and the cathode plate
of an adjacent cell. Conventional bipolar plates may for example be formed from a single
sheet of metal, with machined or pressed features on opposing faces to allow for the
passage of fuel and oxidant.
In so-called pen cathode' fuel cell assemblies, cathode fluid flow channels allow for free
passage of air through the fuel cell assembly, which functions both to supply oxidant to
the individual cells and to provide cooling. A problem with such arrangements is that the
fuel cell assembly needs large amounts of forced air to achieve both functions, and the
cathode channels therefore need to be large to accommodate sufficient air flow.
Reducing the size of such assemblies can be difficult, as the efficiency of cooling by such
means can be compromised by making the cathode channels smaller.
The use of so-called 'closed cathode' fuel cell assemblies addresses the problem of
forced air cooling by instead using dedicated coolant channels provided within the bipolar
plate, while the cathode channels function mainly to provide oxidant. Such coolant
channels may be provided by mating a pair of pre-machined plates together to provide
channels running between the plates. This arrangement allows for coolant fluid, typically
water, to be passed through a bipolar plate when in use, which greatly increases the
efficiency of cooling compared to forced air cooling in open cathode assemblies.
A problem with such closed cathode assemblies, however, is that the complexity of each
individual cell is increased due to the need for additional coolant channels. This can result
in an increase, rather than a decrease, in the overall size of each cell. This also results in
an increased cost for manufacturing each cell.
Other problems to be addressed in fuel cell assemblies include: ensuring a uniform flow
field for fluid distribution in fuel, oxidant and coolant lines; minimising the pressure drop
across inlet manifolds; minimising the sealing pressure required to ensure gas-tight
operation; making the construction of a bipolar plate compatible with mechanised
assembly processes, given the large number of units that need to be assembled with
precision in manufacturing a fuel cell assembly; reducing the pitch of the fuel cells making
up a stack while maintaining operation within desired parameters; reducing the number of
components; reducing the overall weight; reducing material usage and wastage;
simplifying the design, manufacture and assembly; and in general reducing the overall
cost of a fuel cell assembly.
It is an object of the invention to address one or more of the above mentioned problems.
According to one aspect, the present invention provides a fluid flow plate for an
electrochemical assembly, comprising:
a plurality of first fluid flow channels extending across a face of the flow plate to
define a first fluid flow field of the fluid flow plate;
a plurality of second fluid flow channels extending across a face of the flow plate
to define a second fluid flow field of the fluid flow plate, the pluralities of first fluid flow
channels and second fluid flow channels both occupying a common channel plane;
an array of first fluid transfer points disposed along an edge of the first fluid flow
field for communicating fluid into or out of the first fluid flow channels;
an array of second fluid transfer points disposed along an edge of the second fluid
flow field for communicating fluid into or out of the second fluid flow channels;
a first fluid gallery having a first peripheral edge portion bounded by the array of
first fluid transfer points and having a second peripheral edge portion forming a first fluid
communication edge of the fluid flow plate,
a second fluid gallery having a first peripheral edge portion bounded by the array
of second fluid transfer points and having a second peripheral edge portion forming a
second fluid communication edge of the fluid flow plate,
wherein the first fluid gallery occupies a first gallery plane and the second fluid
gallery occupies a second gallery plane different from the first gallery plane, and in which
both the first gallery plane and the second gallery plane are disposed within the channel
plane.
The fluid flow plate may further include:
a plurality of third fluid flow channels extending across the fluid flow plate between
the first face and the second face to define a third flow field of the fluid flow plate, the third
fluid flow channels occupying the common channel plane;
an array of third fluid transfer points disposed along an edge of the third fluid flow
field for communicating fluid into or out of the third fluid flow channels;
a third fluid gallery having a first peripheral edge portion bounded by the array of
third fluid transfer points and having a second peripheral edge portion forming a third fluid
communication edge of the fluid flow plate,
wherein the third fluid gallery occupies a third gallery plane that is different from
the first gallery plane and the second gallery plane and in which the third gallery plane
also is disposed within the channel plane.
The first fluid flow channels may comprise anode fluid flow channels, the second fluid flow
channels may comprise cathode fluid flow channels, the first face may be an anode face,
the second face may be a cathode face; the first fluid gallery may be an anode gallery
and the second fluid gallery may be a cathode gallery. The third fluid flow channels may
comprise coolant fluid flow channels and the third fluid gallery may be a coolant gallery.
The first fluid flow channels may comprise cathode fluid flow channels, the second fluid
flow channels may comprise coolant fluid flow channels; the first fluid gallery may be a
cathode gallery and the second fluid gallery may be a coolant gallery.
The edge of the first fluid flow field and the edge of the second fluid flow field may be
superposed. The edge of the third fluid flow field and the edge of the first fluid flow field
may be superposed. The first fluid communication edge may form part of a first fluid port
extending through the channel plane and the second fluid communication edge may form
part of a second fluid port extending through the channel plane. The third fluid
communication edge may form part of a third fluid port extending through the channel
plane. At least one of the first, second and third fluid communication edges may
comprise an external edge of the plate and at least another one of the first, second and
third fluid communication edges may comprise an internal edge of the plate. At least one
of the first, second and third fluid communication edges may comprise a castellated
structure. At least two of the first fluid gallery, the second fluid gallery and the third fluid
gallery may be at least partially overlapping one another. The first fluid flow channels, the
second fluid flow channels and the third fluid flow channels may be defined by first and
second corrugated plates engaged with one another.
Aspects and embodiments of the invention are described in further detail below by way of
example and with reference to the enclosed drawings in which:
Figure 1 is a perspective view of a bipolar plate separated to show internal coolant
manifold and fluid flow channels, and external cathode manifold and fluid flow channels;
Figure 2 is a perspective view of the reverse face of the bipolar plate of figure 1,
showing anode manifold and fluid flow channels;
Figure 3 is a magnified view of the coolant and cathode manifolds and flow
channels of the bipolar plate of figure 1;
Figure 4 is a magnified view of the anode manifold and fluid flow channels of the
bipolar plate of figure 2;
Figure 5 is a detailed view of a coolant port manifold in one of the corrugated
plates making up a bipolar plate;
Figure 6 is a detailed view of the underlying corrugated plate in the detailed view of
figure 5;
Figure 7 is a sectional view transverse the fluid flow field region of a bipolar plate,
showing the arrangement of interengaging corrugations in the first and second corrugated
plates making up the anode, cathode and coolant fluid flow channels;
Figure 8 is a sectional view of a cathode port and manifold connecting to a series
of cathode fluid flow channels;
Figure 9 is a sectional view of an anode manifold connecting to a series of anode
fluid flow channels;
Figure 10 is a sectional view through a cathode port and cathode manifold;
Figure 1 a is a perspective view of an anode side of a bipolar plate;
Figure 11b is a perspective view of a cathode side of the bipolar plate of figure
11a;
Figure 12a is a detailed sectional view of a transverse fluid connection region in an
assembled bipolar plate;
Figure 12b is an alternative detailed sectional view of a transverse fluid connection
region in an assembled bipolar plate;
Figure 13 is a sectional view through a corrugated region and an anode manifold
region of a bipolar plate;
Figure 14 is an illustration of anode, cathode and coolant fluid volumes within a
bipolar plate;
Figure 15 is a sectional view of the fluid volumes of figure 14;
Figure 16 is a sectional view of a stack comprising five membrane electrode
assemblies and six bipolar plates;
Figure 17 is a partial perspective view of a cathode face of an alternative
embodiment of bipolar plate;
Figure 18 is a partial perspective view of an anode face of the bipolar plate of
figure 17;
Figure 19 is a partial perspective view of a coolant manifold on a reverse of the
anode face of the bipolar plate of figures 17 and 18; and
Figure 20 is a perspective view of a multi-plate assembly of the bipolar plates of
figures 17-19.
Figures 1 to 10 illustrate a first type of bipolar plate, in which an anode fluid flow field
across a face of the plate is in the form of an arrangement of parallel tracks or channels.
Figures 1 to 15 illustrate a second type of bipolar plate, in which the anode fluid flow field
is in the form of a single serpentine track or channel across the face of the plate. These
different embodiments require different arrangements of channels in the bipolar plate, as
described in further detail below.
Figures 1 and 2 show perspective views of an embodiment of a bipolar plate 10. The
bipolar plate 10 comprises first and second corrugated plates 1, 12 that engage together
to form the assembled bipolar plate 10. The first plate 11 comprises a first plurality of fluid
flow channels 13 across a first face of the bipolar plate 10, in the form of corrugations
extending between first inlet and outlet ports 18a, 18b at opposing ends of the bipolar
plate. In the arrangement shown, these ports 18a, 18b are used for the flow of cathode
fluid, i.e. oxidant, through the assembled fuel cell formed from a stack of such plates. The
first plurality of fluid flow channels 13 formed by the corrugations may be alternatively
described as cathode fluid flow channels. A cathode manifold or gallery 15a, 15b is
provided at each end of the plate 10 connecting the respective ports 18a, 18b and the
fluid flow channels 13. The manifolds or galleries 15a, 15b serve to distribute fluid flowing
into and out of the stack through the ports 18a, 18b among the fluid flow channels 13 with
a minimum pressure differential across the width of the plate 10, so as to achieve a
uniform flow of fluid along the channels 13.
Second inlet and outlet ports 19a, 19b are provided at opposing ends of the bipolar plate
10 for flow of fluid into and out of the plate and along a second plurality of fluid flow
channels 22 provided on a second opposing face of the bipolar plate 10, as shown in the
reverse view of the plate in figure 2. These second fluid flow channels 22 may be
described as anode fluid flow channels, and the ports 19a, 19b as anode ports, for the
distribution of fuel gas through and across the bipolar plate 10. Anode manifold regions or
galleries 21a, 21 are provided connecting the anode inlet and outlet ports 19a, 19b to the
second plurality of fluid flow channels 22.
Third inlet and outlet ports 17a, 17b are also provided in the plate 10 for the transmission
of coolant fluid, such as water, into and out of the bipolar plate 10 when assembled into a
fuel cell stack. These ports 17a, 17b communicate, via coolant manifolds or galleries
(only gallery 16b is visible), with a third plurality of fluid flow channels 14 extending
between the third inlet and outlet ports 17a, 17b at opposing ends of the bipolar plate 10.
The third plurality of fluid flow channels 14 are provided between the first and second
corrugated plates 11, 12 forming the first and second opposing faces of the bipolar plate
10. In the embodiment illustrated in figures 1 and 2, corrugations making up the third
plurality of fluid flow channels 14, i.e. the coolant channels, are provided by engagement
of the reverse sides of the corrugations in the plates 11, 2 making up the first and second
plurality of fluid flow channels. This is illustrated in further detail in figure 7, described
below.
The form of the bipolar plate 10 may be fabricated from a single press-formed corrugated
metal plate comprising the first (or cathode) plate 11 and the second (or anode) plate 12,
which may be connected via a fold line. The plates 11, 12 can then be folded together
along the adjoining fold line to interleave the corrugations forming the third set of fluid flow
channels between the plates 11, 12. The press-forming process can also form the ports
17a, 17b, 18a, 18b, 19a, 19b in the same step as forming the fluid flow channels 13, 14,
22.
Applied to faces of each of the corrugated plates , 12 making up the bipolar plate 10 are
gaskets 23a, 23b, 23c, which act to provide fluid seals around the periphery of the
opposing outer faces of the bipolar plate 10 and between the first and second corrugated
plates 11, 12. The gaskets 23a, 23b, 23c are preferably provided in the form of moulded
elastomeric material applied to the faces of the corrugated plates 11, 12. As well as
providing fluid seals around the periphery of the plate 10, and around the periphery of
each of the inlets and outlets, the moulded gasket material provides additional surface
detail to form the inlet and outlet manifolds for each of the fluid flow channels 13, 14, 22,
as shown in further detail in subsequent figures. The patterns in the moulded gaskets
23a, 23b, 23c allow for conduction of air, fuel (hydrogen) and coolant (water) to be
directed from inlet ports to the relevant channels formed in and between the plates 1, 12
and from these channels to exhaust ports. The plates , 12 illustrated in figure 1 and
subsequent figures are symmetrical, so the ports 17a, 18a, 19a or 17b, 18b, 19b can be
considered either inlet or outlet ports. Flow of fluid from each inlet port to the
corresponding outlet port can be in a common direction or in different directions,
depending on the particular implementation.
The anode and cathode manifolds 21a, 21b, 15a, 15b are each shaped to minimise the
pressure drop across the width of the flow fields.
Figure 3 illustrates a magnified view of one end of the bipolar plate 10 of figure 1, showing
the cathode manifold or gallery 15b and the coolant manifold or gallery 16b. The cathode
manifold 15b comprises an open array of raised features formed in the gasket material,
the raised features being configured to provide a defined separation between the bipolar
plate and an adjacent layer (which in this case is the membrane-electrode assembly, or
MEA) while allowing a flow of fluid between the cathode port 18b and the fluid flow field 13
formed by corrugations in the first plate 11. In the embodiment shown, a castellated
region 3 1 of the cathode manifold 15b is disposed along an edge of the manifold region
15b adjoining the port 18b, the castellated region 3 1 serving to direct the flow of fluid into
or out of the manifold 15b while maintaining a required separation along the edge of the
manifold region 15b. In the space between the castellated region and the cathode fluid
flow field 13, the manifold 16b comprises an array of projections 33 in the gasket material
configured to allow free flow of fluid into or out of the corrugations 13.
A similar arrangement of raised features in the gasket material is provided for the coolant
manifold 16b and for the anode manifold 21b, as illustrated in figure 4. Each of the
manifolds 15b, 16b, 21b is provided with a castellated region 31, 32, 34 adjacent the
corresponding port 18b, 17b, 19b and with arrays of projections in the moulded gasket
between the port 17b, 19b and the fluid flow field 22, 14. Each of the manifolds is shaped
to minimise a pressure difference across the corresponding flow field and to maximise the
inlet and outlet area. The combination of generally triangular shaped ports with shaped
manifolds allows for an optimum use of area at each end of the generally rectangular
bipolar plate.
Illustrated in figure 5 is a more detailed perspective view of a region of the second plate
12 around the coolant port 17b, showing the castellated region 32 in the manifold region
along the edge of the port 17b between the port 17b and the coolant fluid flow field 14.
The corrugated plate 12 comprises a central metallic plate 5 1 having a moulded gasket
23a, 23c applied on opposing faces. The moulded gasket 23a on one face of the metallic
plate 5 1 comprises the manifold 16b with the castellated region 32 along an edge
adjoining the port 17b. The gasket material is thicker over the castellated region 32 of the
manifold 16b compared with the periphery of the plate 12, to allow for a larger crosssectional
area for fluid to enter or exit the manifold. This is made possible by offsetting
the metallic plate 5 1 under the castellated region 32. This is illustrated more clearly in
figure 6, which shows the metallic plate 5 1 without the gasket layers 23a, 23c applied. An
offset is provided in the plate 5 1 by means of a debossed region 6 1 extending across an
edge of the coolant port 17b. A similar arrangement may be applied in relation to the
cathode and anode ports and manifolds.
Figure 7 illustrates a transverse sectional view across the bipolar plate 11, indicating the
arrangement of corrugations allowing for fluid flow channels across the anode, cathode
and coolant fluid flow fields to be coplanar. Anode fluid flow channels 72 are provided by
corrugations in the second corrugated plate 12, comprising the metallic plate 5 1 and
gasket layers 23b, 23c. Cathode fluid flow channels 73 are provided by corrugations in
the first corrugated plate 11, comprising metallic plate 7 1 and the gasket layer 23a. The
gasket layer 23b may instead be applied to the first corrugated plate 11 to achieve the
same result.
Coolant channels 74 are provided by openings in the space between the metallic plates
71, 5 1 of the first and second corrugated plates 11, 12. In the embodiment illustrated, the
coolant channels 74 are formed between the first and second corrugated plates 1 , 12 by
omission of selected corrugations in the second plate 12. The same effect may be
achieved by omission of selected corrugations in the first plate 11. The coolant channels
are preferably uniformly distributed across the width of the bipolar plate 10, and provided
by omission of alternate corrugations in the second plate 12. In alternative arrangements,
the coolant channels may be formed between the first and second corrugated plates by
narrowing or by a height reduction of selected corrugations in the first or second plate.
The arrangement of coolant channels in the bipolar plate allows for an efficient use of both
space and material, since the corrugations providing fluid flow channels in the anode and
cathode sides of the plate also serve to define a further set of fluid flow channels for
coolant between the corrugated plates.
The channels 72, 73, 74 on and between the corrugated plates 5 1, 7 1 are shown in figure
7 as being parallel to each other and substantially uniform along the length of the bipolar
plate 10. In alternative embodiments, the channels may be non-parallel and may for
example be tapered or varied in dimensions to account for expected pressure or
temperature variations across the bipolar plate 0 in use.
Figure 8 shows a detailed sectional view of the bipolar plate, illustrating features of the
cathode port 18b and cathode manifold 15b. As for the coolant manifold, illustrated in
figure 5 and described above, the cathode manifold 15b comprises a castellated region 3 1
formed in the gasket 23a along an edge of the manifold 15b adjoining the cathode port
18b. Cathode fluid (i.e. oxidant and water) entering or exiting the cathode fluid flow field
formed by corrugations 13 is directed to or from the port 18b through the castellated
region 31, which functions to maintain a separation between the underlying metallic plate
5 1 and an against which the first face of the bipolar plate is in contact when
assembled into a fuel cell stack.
Figure 9 illustrates a detailed sectional view through the anode manifold region 21b, in
which a section of the castellated region 3 1 of the cathode manifold can also be seen.
The anode manifold region 21b is typically of smaller thickness than the cathode manifold
region 15b, since a greater flow of fluid is required through the cathode fluid flow field than
through the anode fluid flow field.
Figure 10 illustrates a further sectional view through the cathode manifold region 15b, in
which the coolant manifold 16b can be seen sandwiched between the metallic plates 51,
71. The debossed region 6 1 corresponding to the castellated region 32, described above
in relation to figures 5 and 6, can also be seen in this view.
In the above described embodiment, the anode fluid flow field is provided in the form of a
plurality of parallel channels formed by corrugations in the first corrugated plate 11. In
alternative embodiments the anode fluid flow field in the first corrugated plate may be
provided in the form of a serpentine track extending across the first face of the bipolar
plate. Figures 11a and 11b illustrates such an embodiment, where the bipolar plate 1 11
comprises a first face (figure 11a) having an anode fluid flow field 122 in the form of a
single serpentine track extending between anode inlet and outlet ports 119a, 19b and a
second face (figure 1 ) having a cathode fluid flow field 1 3 in the form of an array of
interdigitated corrugations extending between cathode inlet and outlet ports 118a, 118b.
The main differences as compared with the embodiment illustrated in figures 1 to 10 are
the inclusion of transverse connecting regions 126 provided at opposing ends of the plate,
forming fluid connections between adjacent anode fluid flow channels to allow the anode
fluid flow channels to together form a single track between the anode inlet and outlet ports
119a, 119b.
The transverse connecting regions 126 are illustrated in more detail in figures 12a and
12b, which respectively illustrate detailed sectional views of the second and first faces of
the bipolar plate 111 through one such transverse connecting region. A return path is
provided by each transverse connecting region 126 to connect adjacent anode fluid flow
channels 122. To allow for coolant to pass between the plates 171 , 151 between the
coolant manifold 16 and each coolant channel 128, each transverse connecting region
126 has a depth that is less than the depth of the adjacent anode channels. Coolant can
then pass beneath each transverse connecting region 126 and along the coolant channels
28. To support the connecting regions, a plinth 125 is provided on the cathode fluid flow
field, and a point of connection 127 is provided between the metallic plates 151, 171. The
point of connection 127 may be a spot weld between the plates 151, 171, serving to
maintain the relative position of the plates and transmit pressure through the thickness of
the plates 151, 171 without collapsing the return path 126 or the coolant flow field 128
provided between the plates. Each plinth 125 acts as a barrier between a longitudinally
adjacent cathode fluid flow channel 113b and an adjacent cathode manifold region 115a,
thereby separating the cathode flow channels into inlet channels 113a (connected to the
cathode manifold 115a) and exhaust channels 13b (connected to the cathode manifold
115b) and forming the cathode fluid flow field 113 into an array of interdigitated channels.
Fluid passing from the cathode inlet port 118a passes across the cathode manifold 115a
and into the inlet channels 113a. Fluid then passes along the inlet channels 113a and
diffuses through the gas diffusion layer (not shown) and into the outlet channels 113b.
Fluid then passes along the cathode outlet channels 113b and along the outlet channels
113b into the outlet manifold 115b and out of the plate 1 1 through the cathode outlet port
118b.
In a general aspect therefore, the second face of the bipolar plate may comprise a fluid
flow field 113 in the form of an array of interdigitated fluid flow channels 113a, 113b
formed by corrugations in the second face of the bipolar plate 1 1 1. Barriers 125 may be
provided at opposing ends of the interdigitated fluid flow channels, each barrier 125
configured to form a fluid seal between an adjacent longitudinal fluid flow channel 113a,
113b and an adjacent inlet or outlet manifold 115b, 115a.
Figure 13 illustrates a cutaway perspective view of a section of the bipolar plate 111, in
which the transverse connecting regions 126 are shown connecting adjacent pairs of
anode channels 122. Coolant channels 174 can also be seen extending longitudinally
between the corrugated plates 151, 171. Each coolant channel 174 extends along the
bipolar plate 1 11 between a pair of adjacent anode channels 122 and connects to the
coolant manifold 16 via a gap between the plates 151, 171 beneath a transverse
connecting region 126.
Figure 14 illustrates a perspective view of the spaces between the plates making up the
bipolar plate 111 of figure 11, corresponding to a coolant volume 141, a cathode volume
142 and an anode volume 143. A more detailed view of a portion of these volumes is
provided in figure 5, illustrating sections taken parallel and transverse to the corrugations
in the plate. These exemplary views illustrate a general principle according to an aspect
of the invention of transferring fluids from the various ports 141, 142, 143 with a minimal
pressure drop and with a uniform distribution to each of the fluid flow fields across the
bipolar plate. This is achieved by maximising the length of the inlet of each manifold
region and by overlapping the manifold regions through the plate. The use of an open
array of raised features (described above in relation to figures 3 and 4) allows for the
manifold regions to be overlapping while maintaining a separation between adjacent
plates to allow for fluid flow in an assembled fuel cell stack. This aspect will be described
in detail later.
Figure 16 illustrates a sectional view through a fuel cell stack 160 comprising five MEA
layers and six bipolar plates 111 of the type illustrated in figure 11. In each bipolar plate
111 a cathode plate 151 is bonded to an adjacent anode plate 171 by means of a spot
weld 127 connecting the plinth or barrier 125 in the cathode plate 151 with the
corresponding transverse connecting region 126 in the anode plate (described above in
relation to figures 12a, 12b). Anode and cathode plates in adjacent bipolar plates are
separated by a membrane electrode assembly (MEA) 162 having a cathode gas diffusion
layer 163 on one face and an anode gas diffusion layer 164 on the other face. The MEA
162 extends beyond the extent of the gas diffusion layers 163, 164, the MEA overlaying
the cathode manifold, 115, anode manifold 121 and the coolant manifold 16 between the
anode and cathode plates 151, 171. The cathode port 118 is indicated in figure 16,
connected to the cathode manifold 15 via a castellated region 131 in each bipolar plate
making up the stack 60.
Figures 17, 18 and 19 illustrate a further alternative embodiment of a bipolar plate 210.
Figure 17 shows the cathode face of the plate 210, figure 18 the anode face and figure 19
the reverse of the anode face indicating the coolant manifold and channels. In this
embodiment, the cathode ports 218 are provided by an external enclosure (not shown),
which provides an air flow through a pair of cathode air inlets to or from a cathode
manifold region 215, the cathode air inlets being provided on an outer periphery or
external edge 3 1 of the bipolar plate 210. As with the embodiments described above,
the bipolar plate 210 comprises an anode port 219 in fluid communication with an anode
manifold region 221 (shown in figure 18), and a coolant port 217 in fluid communication
with a coolant manifold region 216 (shown in figure 19). The anode, cathode and coolant
fluid flow regions across the plate 210 are otherwise similar to the embodiment described
above in relation to figures 11 to 16. In this embodiment, the cathode air inlet (or outlet) is
configured to be substantially larger in cross-sectional area than either of the coolant or
anode inlets or outlets, thereby allowing a greater volume flow rate of air through the plate
210 in use. The anode inlet or outlet, which is defined by the size of the anode port 219,
is substantially smaller than either of the cathode or coolant inlets, since the volume of
fluid passing in or out of the anode port is smaller.
In a general aspect, according to the embodiment illustrated in figures 17-19 the second
inlet and outlet ports 218 are provided on a peripheral edge of the bipolar plate 210,
whereas the first and third inlet and outlet ports 219, 217 are provided through the
thickness of the bipolar plate 210. An advantage of this arrangement is that the second
(cathode) inlet and outlet ports can be made substantially larger, allowing a greater flow of
oxidant fluid into and out of the fuel cell made up of a stack of such bipolar plates.
In this embodiment, unlike the embodiments described above in relation to figures 1 to 16
where the manifold regions are partially overlapping, the manifold regions 215, 216, 221
of the plate 210 in figures 17-19 are entirely overlapping due to the cathode port being
provided on the periphery of the plate, thereby allowing for a more uniform pressure
distribution across the width of the fluid flow regions of the plate 210. The overlapping
manifold regions also allows for a more uniform seal to be made around the peripheral
edges of each of the manifold regions.
An important feature of embodiments described above is the ability to provide
substantially increased lengths of fluid communication edge of the bipolar fluid flow plate.
Firstly, each of the cathode galleries or manifolds 15a, 15b (figure 1), 1 5a, 115b (figure
1b), 215 (figure 17) can provide fluid communication and distribution between a cathode
fluid port 18a, 18b, 118a, 118b, 218 disposed at an end of the flow plate and a set of
cathode fluid flow channels 3, across a substantially full width of the flow field active area
of the plate defined by those channels.
Secondly, and correspondingly, each of the anode galleries or manifolds 21a, 21b (figure
2), 121a, 121b (figure 11a), 221 (figure 18) can provide fluid communication and
distribution between an anode port 19a, 19b, 119a, 119b, 219 disposed at an end of the
flow plate and a set of anode fluid flow channels 22, across a substantially full width of the
flow field active area of the plate.
Thirdly, and correspondingly, each of the coolant galleries or manifolds 16b (figures 1 and
3) , 216 (figure 19) can provide fluid communication and distribution between a respective
port 17a, 17b, 117a, 117b, 217 disposed at an end of the flow plate and a set of coolant
flow channels 14, across a substantially full width of the flow field active area of the plate.
Each of the galleries (e.g. 15, 21, 16) has a first peripheral edge portion bounded by an
array of fluid transfer points disposed along an edge of the flow field defined by the flow
channels 13, 14, 22. These fluid transfer points are exemplified by the channel ends
indicated at 301, 302, 303 respectively for cathode fluid transfer points, coolant fluid
transfer points and anode fluid transfer points. Each of the galleries (e.g. 15, 21, 16) also
has a second peripheral edge portion disposed along an edge of the flow plate, described
herein as a fluid communication edge 320, 321, 322. The fluid communication edge
provides for delivery of fluid into the gallery (or egress of fluid from the gallery) by way of
the plate edge that forms part of a side wall of the respective port, e.g. cathode fluid ports
18, 18b, 18a, 1 8b, 218; anode fluid ports 19a, 19b, 119a, 1 9b, 219; and coolant fluid
ports 17a, 17b, 7a, 117b, 217. These fluid communication edges 320, 321, 322 are
exemplified by the castellated regions 31, 32, 34, 131, 132, 34.
The first peripheral edge portions of each gallery are generally superposed on one
another because the cathode flow channels 3, coolant flow channels 14 and anode flow
channels 22 all generally define substantially the same active area, or flow field, of the
bipolar plate 0. However, the second peripheral edge portions (e.g. castellated regions
3 1, 32, 34, 131, 132, 134) may not be superposed on one another as this would conflict
with the requirement that the fluid communication edges define parts of the side walls of
separate fluid delivery ports extending through the planes of the bipolar plates in the fuel
cell stack. For optimal distribution of fluids into the bipolar plate, it is beneficial to have the
maximum possible length of second peripheral edge portions 31, 32, 34, 131, 132, 134 for
each gallery 15, 21, 16. Thus, there exists a challenge to increase the total length of fluid
communication edge of the bipolar plate for any given length of fluid transfer points (i.e.
width of the active flow field area).
Each of the embodiments described above achieves a degree of extension of the total
length of fluid communication edges 320, 321 , 322 (second peripheral edge portions of
the galleries) compared with the length of the fluid transfer points (corresponding to the
lengths of any of the first peripheral edge portions of the cathode gallery 15, anode gallery
2 1 or coolant gallery 16).
In the arrangement of figures 1 to 4, it can be seen that the triangular configurations of
cathode ports 18, anode ports 19 and coolant ports 17 and their relative positions,
together with the corresponding generally triangular shaping of the respective cathode
galleries 15, anode galleries 2 1 and coolant galleries 16 achieves a combined length of
second peripheral edge portions 3 1, 32, 34 that is greater than the length of the first
peripheral edge portion (i.e. the active area or flow field width) of any one of the cathode,
anode or coolant galleries. In fact, the design sufficiently extends the lengths of the fluid
communication edges that the combined length of second peripheral edge portions 31, 32
for the cathode and coolant flows is greater than the length of the first peripheral edge
portion of any of the cathode gallery 15, anode gallery 2 1 or coolant gallery 16.
In the arrangement of figures 11a and 11b, it can be seen that the ports 117, 118, 19 are
extended to provide greater volume, but each includes at least one edge portion (e.g.
castellated region 131, 132, 134) which is oblique to the first peripheral edge portion (e.g.
at fluid transfer points 301, 302, 303), thereby providing each of the galleries 115, 121,
116 with at least one portion which is generally triangular in shape. In these galleries, the
first peripheral edge portion may form the base of a triangle, while the second peripheral
edge portion may form a side of the triangle. Other more complex shapes are possible.
It will also be noted from figure a that if the anode flow field 122 is provided as a single
serpentine channel extending from a single channel opening at each end of the plate,
there will only be a single fluid transfer point 303 and no need to extend the anode gallery
121 across the full flow field 122 width and it may not be necessary to have an anode
gallery. However, the principles described with respect to an anode gallery 121 having a
first peripheral edge portion extending across the width of the anode flow field can still
apply where multiple serpentine channels are provided.
In a general aspect, the total length of fluid communication edges 320, 321, 322 can be
achieved by presenting at least one, and preferably more than one, of the second
peripheral edge portions of one or more of the galleries 15, 21, 16 at an oblique angle to
the first peripheral edge portions of the galleries.
In another aspect, the total length of fluid communication edges can be increased further
by using both internal and external edges of the bipolar plate to form fluid communication
edges. It can be seen that the exemplary arrangements in figures 1 to 4 and figures 11a
and 1 b each provide fluid communication edges defined on an internal edge of the plate,
i.e. an edge of the plate defined within a hole or aperture passing through the plate 10,
1 1 1. In the arrangement of figures 17 to 19, an even greater length of fluid
communication edge is provided by using both internal and external edges of the plate.
Coolant fluid port 217 and anode fluid port 219 both define internal edges 310 of the
bipolar plate 210. However, cathode fluid is delivered by an external edge 311 where the
fluid is constrained within a cathode port 218 by an external enclosure discussed earlier.
In this type of arrangement, a flow field width (i.e. the length of first peripheral edge
portion or plate width across all channels) of 40 mm has been provided with a
corresponding total port length (i.e. total length of second peripheral edge portions for all
galleries) of 120 mm. This is made up of a cathode port 218 castellated region 231 of 60
mm, an anode port 219 castellated region 234 of 20 mm (circumferential) and a coolant
port 217 castellated region 232 of 40 mm. Thus, the ratio of fluid communication edge
(total of all second peripheral edge portions) to f ow field width (first peripheral edge
portion) of at least 2:1 and preferably 3:1 or more is possible in this arrangement. More
generally the ratio of fluid communication edge (second peripheral edge portion) of one
gallery to the first peripheral edge portion of the gallery can be 1.2:1 or even as high as
1.5:1 in the example of figures 17-19.
In preferred arrangements, the ratio of fluid communication edges for each of the cathode
: anode : coolant is preferably of the order of 50% : 6% : 34%. However, other ratios can
be selected according to the design parameters of the fuel cell stack. The castellated
structures 31, 32, 34, 131 , 132, 134 can provide any suitable aspect ratio of open to
closed to optimise flow rates versus supporting strength against compression of the
gasket layers, but a 50% : 50% aspect ratio is found to be optimal with certain designs.
In practice, it is often found that cathode fluid flows and coolant fluid flows are the largest
and / or most critical and therefore maximizing the lengths of fluid communication edges
for the cathode and coolant galleries at the expense of reduced fluid communication
edges for the anode galleries can be beneficial.
Another important feature of the embodiments described above is the ability to feed two or
three different fluids into two or more of coplanar anode, cathode and coolant channels
72, 73, 74 (figure 7) or 22, 13, 14 (figures 1 and 2). Fluids are delivered to a stack of
plates 10 by ports passing through the planes of the plates. These ports are seen in
figures 1 and 2 comprising anode ports 19a, 19b, cathode ports 18a, 18b and coolant
ports 17a, 17b. Thus, if the plane of the plate 10 is said to lie in an x-y plane, the ports all
extend in the z-direction but are spatially separated from one another in the x-y plane.
The galleries delivering fluids should preferably all extend across the full width (xdirection)
of the flow field of the plates, while being separated at their fluid communication
edges with the ports 17, 18, 19. This can be achieved by providing three different levels,
or planes, of galleries all of which occupy one common level, or plane, of the coplanar
anode, cathode and coolant channels. The expression "plane" or "level" in this context is
intended to specify a finite space along the z-dimension. The anode channels 72,
cathode channels 73 and coolant channels 74 occupy a common plane, level or "z-space"
referred to as the channel plane. The anode gallery 21a, 21b, 121a, 121b, 221 occupies
a thinner plane within the channel plane, but different from a plane occupied by the
cathode gallery 15a, 15b, 115a, 115b, 215. The coolant gallery 16b, 216 occupies a
plane within the channel plane but different from either the anode gallery plane and the
cathode gallery plane.
With reference to figure 8, it can be seen that the cathode gallery 15b has an array of first
fluid transfer points 301 where it meets the ends of the cathode fluid flow channels 13 at
the edge of the cathode fluid flow field defined by the channels 13. This can be
considered to be a first peripheral edge portion of the gallery which extends across the
flow field width. The cathode gallery 15b also has a second peripheral edge portion
defined by the castellated region 3 1 which forms a fluid communication edge 320 by
which cathode fluid can flow between the cathode port 18b and the cathode gallery 15b.
With further reference to figure 5, it can be seen that the coolant gallery 16b has an array
of fluid transfer points 302 where it meets the ends of the coolant fluid flow channels 14 at
the edge of the coolant fluid flow field defined by the channels 14. This can be considered
to be a first peripheral edge portion of the coolant gallery 16b which extends across the
flow field width. The coolant gallery 16b also has a second peripheral edge portion
defined by the castellated region 32 which forms a fluid communication edge 321 by
which coolant fluid can flow between the coolant port 17b and the coolant gallery 6b.
With further reference to figure 4, it can be seen that the anode gallery 21b has an array
of fluid transfer points 303 where it meets the ends of the coolant fluid flow channels 22 at
the edge of the coolant fluid flow field defined by the channels 22. This can be considered
to be a first peripheral edge portion of the anode gallery 21b which extends across the
flow field width. The anode gallery 21b also has a second peripheral edge portion defined
by the castellated region 34 which forms a fluid communication edge 322 by which anode
fluid can flow between the anode port 19b and the anode gallery 21b.
Similar examples of the cathode fluid communication edge 320, the coolant fluid
communication edge 321 and the anode fluid communication edge 322 are also shown in
figures 17 to 19. It will be seen that each of these communication edges occupies a
slightly different z-position and forms part of the wall of the respective anode port, cathode
port and coolant port.
Figure 20 shows an arrangement in which multiple plates 350a, 350b, 350c, 350d can be
formed side-by-side from a single sheet of material. The side-by-side configuration can
be used to form extra wide plates split into different flow field regions each served by its
own respective set of cathode, anode and coolant ports (e.g. coolant ports 217a - 217d),
and its own respective set of anode, cathode and coolant galleries. Alternatively, the sideby-
side configuration can be used to form plates 350a, 350b connected by a fold line as
discussed earlier, such that adjacent plates 350a, 350b respectively comprise an anode
plate and a cathode plate which can be folded over one another to create the bipolar
plate.
The embodiments shown in the figures all relate to bipolar plates in which an anode flow
field (defined by channels 22) is provided on one face of the plate 0 and a cathode fluid
flow field (defined by channels 13) is provided on another face of the pate, while a coolant
fluid flow field (defined by channels 14) is provided within the plate. The principles of
extending the combined lengths of second peripheral edge portions 31, 32, 34 of at least
two of the fluid galleries 15, 16, 2 1 compared to the length of the first peripheral edge
portion (bounded by the fluid transfer points 301 , 302 or 303) can also be deployed in a
monopolar plate, e.g. where only a cathode flow field and a coolant flow field is required.
In such circumstances the anode flow field could be provided by a separate plate.
Similarly, the principles of disposing at least two second peripheral edge portions 31, 32,
34 at oblique angles to the first peripheral edge portion (bounded by the fluid transfer
points 301, 302 or 303) to provide a total length of the array of second fluid transfer points
that is at least as long as, and preferably longer than, the length of the array of first fluid
transfer points can also be deployed in a monopolar plate, e.g. where only a cathode flow
field and a coolant flow field is required. In such circumstances the anode flow field could
be provided by a separate plate.
Similarly, the principles of providing a first fluid gallery which occupies a first gallery plane
and a second fluid gallery which occupies a second gallery plane different from the first
gallery plane, and in which both the first gallery plane and the second gallery plane are
disposed within a channel plane can be deployed in a monopolar plate where the first and
second fluid galleries are to supply cathode fluid and coolant fluid. In such circumstances
the anode flow field could be provided by a separate plate.
Other embodiments are intentionally within the scope of the invention as defined by the
appended claims.
CLAIMS
1 A fluid flow plate for an electrochemical assembly, comprising:
a plurality of first fluid flow channels extending across a face of the flow plate to
define a first fluid flow field of the fluid flow plate;
a plurality of second fluid flow channels extending across a face of the flow plate
to define a second fluid flow field of the fluid flow plate, the pluralities of first fluid flow
channels and second fluid flow channels both occupying a common channel plane;
an array of first fluid transfer points disposed along an edge of the first fluid flow
field for communicating fluid into or out of the first fluid flow channels;
an array of second fluid transfer points disposed along an edge of the second fluid
flow field for communicating fluid into or out of the second fluid flow channels;
a first fluid gallery having a first peripheral edge portion bounded by the array of
first fluid transfer points and having a second peripheral edge portion forming a first fluid
communication edge of the fluid flow plate,
a second fluid gallery having a first peripheral edge portion bounded by the array
of second fluid transfer points and having a second peripheral edge portion forming a
second fluid communication edge of the fluid flow plate,
wherein the first fluid gallery occupies a first gallery plane and the second fluid
gallery occupies a second gallery plane different from the first gallery plane, and in which
both the first gallery plane and the second gallery plane are disposed within the channel
plane.
2. The fluid flow plate of claim 1 further including:
a plurality of third fluid flow channels extending across the fluid flow plate between
the first face and the second face to define a third flow field of the fluid flow plate, the third
fluid flow channels occupying the common channel plane;
an array of third fluid transfer points disposed along an edge of the third fluid flow
field for communicating fluid into or out of the third fluid flow channels;
a third fluid gallery having a first peripheral edge portion bounded by the array of
third fluid transfer points and having a second peripheral edge portion forming a third fluid
communication edge of the fluid flow plate,
wherein the third fluid gallery occupies a third gallery plane that is different from
the first gallery plane and the second gallery plane and in which the third gallery plane
also is disposed within the channel plane.
3. The fluid flow plate of claim 1 or claim 2 in which the first fluid flow channels
comprise anode fluid flow channels, the second fluid flow channels comprise cathode fluid
flow channels, the first face is an anode face, the second face is a cathode face; the first
fluid gallery is an anode gallery and the second fluid gallery is a cathode gallery.
4. The fluid flow plate of claim 3 when dependent from claim 2 in which the third fluid
flow channels comprise coolant fluid flow channels and the third fluid gallery is a coolant
gallery.
5. The fluid flow plate of claim 1 or claim 2 in which the edge of the first fluid flow
field and the edge of the second fluid flow field are superposed.
6. The fluid flow plate of claim 5 when dependent on claim 2 in which the edge of the
third fluid flow field and the edge of the first fluid flow field are superposed.
7. The fluid flow plate of claim 1 or claim 2 in which the first fluid communication
edge forms part of a first fluid port extending through the channel plane and the second
fluid communication edge forms part of a second fluid port extending through the channel
plane.
8. The fluid flow plate of claim 7 when dependent from claim 2 in which the third fluid
communication edge forms part of a third fluid port extending through the channel plane.
9. The fluid flow plate of claim 7 or claim 8 in which at least one of the first, second
and third fluid communication edges comprises an external edge of the plate and at least
another one of the first, second and third fluid communication edges comprises an
internal edge of the plate.
10. The fluid flow plate of claim 1 or claim 2 in which at least one of the first, second
and third fluid communication edges comprise a castellated structure.
1 . The fluid flow plate of claim 1 or claim 2 in which at least two of the first fluid
gallery, the second fluid gallery and the third fluid gallery are at least partially overlapping
one another.
12. The fluid flow plate of claim 2 in which the first fluid flow channels, the second fluid
flow channels and the third fluid flow channels are defined by first and second corrugated
plates engaged with one another.
13. A fluid flow plate for an electrochemical fuel cell assembly substantially as
described herein and with reference to the accompanying drawings.