Title of Invention

BIPOLAR PLATE FOR ELECTROLYSER COMPRISING A SINGLE WALL

Abstract It is described a bipolar plate consisting of a single wall and a perimetrical sealing frame obtained by folding and provided with a planar abutment surface for the frame-to-wall welding. The wall in further provided with projections on one face thereof preferably obtained by moulding and with supports on the other face consisting of sheet strips housed in the recesses formed by the concave part of the projections. The projections substantially extend along the entire length of the bipolar plate. The projections and supports are connected to electrodes or current distributors. The projections, the supports, the single wall and the perimetrical frame are made of the same metal or alloy. The electrode or current distributor supported by the projections, the same projections and the supports are welded together by a single pass of are-welding or preferably laser-welding. The electrode or current distributor connected to the support and the support themselves are mutually welded by a subsequent pass of the welding or preferably laser-welding. The welding between wall and perimetrical frame on the abutment surface of the frame is carrier out by diode-laser technique, allowing to obtain a robust connection but without a complete melting of the sheet, thereby eliminating the risk of process fluid leakage to the external environment.
Full Text WO 2006/053768 PCT/EP2005/012381
BIPOLAR PLATE FOR ELECTROLYSER COMPRISING A SINGLE WALL
BACKGROUND OF THE INVENTION
The electrochemical technology is at the basis of several processes of industrial
relevance, such as the production of aluminium from molten salts, of copper, zinc,
nickel, cobalt and lead from aqueous solutions obtained by leaching of ores, of
chlorine and caustic soda from sodium chloride solutions, of chlorine and
optionally hydrogen from hydrochloric acid solutions and of hydrogen and oxygen
from alkaline or acidic aqueous solutions.
In particular, in the case of chlorine-caustic soda electrolysis:
2 NaCI + 2 H2O→Cl2 + H2 + 2 NaOH
the industrial reactor known as electrolyser consists, in the technologically most
advanced version of membrane electrolysis, of an assembly of elementary cells,
each formed by two shells provided with perimetrical frames equipped with
sealing gaskets, one membrane, two electrodes respectively known as anode and
cathode secured to suitable supports and several nozzles for feeding the reactant-
containing solutions and for discharging the products and the exhaust solutions.
The membrane subdivides the internal volume of each elementary cell into two
compartments, respectively the anodic one, containing the first of the two
electrodes (anode) or current distributors (anodic) secured to the relevant
supports, and the cathodic one containing the first of the two electrodes (cathode)
or current distributors (cathodic) also secured to the relevant supports. Since the
solutions, the reactants and the products present in the two compartments, being
different (respectively sodium chloride solution and chlorine in the anodic
compartment and caustic soda solution and hydrogen in the cathodic
compartment) are characterised by a substantially different chemical
aggressiveness, the construction materials of the two shells cannot be the same:
in particular the anodic shell is built with titanium sheet and the cathodic shell with
nickel sheet.
When the single cells are assembled in electrical series to make up the
electrolyser, the titanium anodic wall of one cell comes in contact with the nickel

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cathodic wall of the subsequent cell.
For a correct understanding of the content of the present invention, which will be
illustrated in the following paragraphs, it is necessary to remind that from a
constructional standpoint each elementary cell may be implemented as an
independent unit consisting of a pair of shells, respectively cathodic and anodic,
for instance as illustrated in DE 19816334 (constructive concept known to the
experts in the field as "single cell").
According to an alternative embodiment the elementary cell does not exist as
independent unit, but is generated instead by the matching of suitable elements
(known to the experts in the field as bipolar plates) when the electrolyser is
assembled, as shown for instance in figure 3 of US 4,767,519. In the case of
chlorine-caustic soda electrolysis each bipolar plate comprises an anodic shell of
titanium and a cathodic shell of nickel coupled in correspondence of the walls, for
example by welding. During the assemblage of a similar kind of electrolyser the
bipolar plates with the membranes and the perimetrical gaskets intercalated in-
between are compressed one against each other: it is in this moment that the
matching of the titanium anodic shell with the nickel cathodic shell of the
subsequent bipolar plate forms the elementary cells.
In the case of alkaline water electrolysis:
2 H2O→ 2 H2 + O2
the two compartments, anodic and cathodic both contain a potassium hydroxide
solution whose aggressiveness is not sensibly influenced by the presence of
oxygen in the anodic compartment and of hydrogen in the cathodic one. Hence
the two shells delimiting each elementary cell are usually made of the same
material, nickel in particular, which is notoriously the metal characterised by best
chemical resistance to alkaline solutions. This aspect has no effect at all in case
the "single cell" design is adopted, while it brings to substantial constructional cost
savings of the bipolar plates: in this case in fact the bipolar plate does not consist
anymore of two mutually welded shells, as illustrated in the case of chlorine-
caustic soda electrolysis, but rather of a single nickel sheet acting, once
assembled the electrolyser, on one side as anodic wall delimiting the anodic

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compartment of one cell and on the other side as cathodic wall delimiting the
cathodic compartment of the subsequent cell (single wall hereafter).
A totally equivalent situation occurs in the case of membrane water electrolysis,
wherein the two solutions, anodic and cathodic, respectively consist of water and
oxygen in the anodic compartment and of water and hydrogen in the cathodic
compartment or, in a special process alternative, of water and oxygen in the
anodic compartment and of humid hydrogen in the cathodic compartment. In both
cases the construction material suited to both the anodic and cathodic conditions
may be stainless steel, or preferably titanium considering its better chemical
inertia.
A further situation, wherein the construction material compatible with both fluids,
anodic and cathodic, may be the same, is given by hydrochloric acid electrolysis
in its two variants, the conventional one with chlorine and hydrogen evolution:
2 HCI → H2 + Cl2
or the oxygen cathode-depolarised one:
4 HCI + O2 -> 2 Cl2 + 2 H2O
In both cases titanium and preferably some alloys thereof turn out to be
compatible with the process conditions of both compartments, anodic (chlorine-
containing hydrochloric acid solution) and cathodic (respectively hydrogen or
oxygen with minor amounts of slightly acidic water). Thus, also in this case the
bipolar plate may comprise a single sheet which during the electrolyser operation
acts as anodic wall on one side and as cathodic wall on the other (see for
instance US 5,770,035).
A restraint to the adoption of the single wall bipolar plate design comes from the
need of the two compartments, cathodic and anodic, to be provided with
perimetrical flanges allowing to seal the same compartments, in co-operation with
suitable gaskets, preventing the leakage of process fluids. In accordance with the
known constructive procedures the perimetrical flanges are either obtained by
moulding or by folding of the sheets constituting the compartment walls: in the
case of bipolar plates comprising a pair of shells respectively destined to delimit
an anodic compartment and a cathodic compartment, as happens in the case of

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the chlorine-caustic soda electrolysis, each wall is processed to form only its own
flange and this operation gives in general satisfying results in terms of planarity
and of absence of mechanical defects. Conversely in the case of bipolar plates
comprising a single wall it is necessary to proceed, operating with the known
procedures, to a double forming since both flanges, cathodic and anodic, are
necessarily part of the same wall. The double forming, independently from the fact
that it is accomplished by moulding or by folding, introduces high mechanical
stresses in the material with remarkable distortions and/or frequent mechanical
defects such as tears.
The problem is tackled in EP 1 366 212, where several types of perimetrical
frames suitable for being used with bipolar plates comprising a single wall are
described. In particular, it is proposed the use of a frame consisting of a bar or
tube both with quadrangular profile, on a face of which the single wall of the
bipolar element is welded, optionally in two subsequent passes in order to better
ensure the absence of defects capable of releasing the process fluids to the
external environment. In a further embodiment, the single wall is processed by
moulding or folding so as to form a single flange, for instance the anodic flange,
while the second flange, for instance the cathodic flange, is preassembled by
moulding or folding of a suitable strip of identical material as that of the single
wall: the preassembled cathodic flange is then secured by welding to the single
wall already provided with the anodic flange. A further manufacturing alternative
proposed as well in EP 1 366 212 provides that both flanges, anodic and cathodic,
be preassembled in form of U-profiled frame obtained by moulding or folding of a
suitable strip and that the single wall, completely planar, be secured, for instance
by welding, in the middle of the frame. The problem of both manufacturing
procedures is given by the need that the welds, whose linear development is
remarkable, present no defect of a size such as to allow the outflow of the process
fluids to the external environment. It follows that the procedure requires
exasperated quality controls, moreover with the frequent intervention of the
operators to eliminate the detected defects. All in all the construction turns out to
be too expensive and not compatible with marketing requirements.

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The above considered production cost aspect is further influenced by the securing
procedures of the anodes and the cathodes, which comprise the production of the
relevant supports and the execution of the required welds.
The reduction of the latter costs was considered in WO 03/038154, which
proposes to obtain the supports for the anodes and cathodes directly from the
single wall through the moulding of projections, for instance of prismatic shape, on
both faces. The anodes and cathodes are subsequently secured on the top of the
projections, for example by welding: the above described procedure allows a
saving since the support material is given by the single wall and the required
welds are reduced to those for securing the anodes and the cathodes on the tops
of the projections getting rid of the wall to support welds, which are needed when
the supports are preassembled separately, as customary in the conventional
constructions. The drawback which prevents from advantageously using the
manufacturing procedure of WO 03/038154 is given by the remarkable
deformation undergone by the sheet of the single wall during the moulding of the
projections on both faces, with the consequence of a totally unacceptable
planarity for bipolar plates which have to be assembled in a high number to form
the industrial electrolysers.
The survey of the prior art thus allows stating that the production of bipolar plates
comprising a single wall, provided with anodic and cathodic flanges as well as of
electrodes or current distributors with the relevant supports and characterised by
suitable planarity and acceptable production costs on the commercial standpoint
certainly represents an industrially relevant problem, with no viable solution so far.
OBJECTS OF THE PRESENT INVENTION
The present invention intends to solve the above outlined problem proposing a
bipolar plate design comprising a single wall provided with flanges, anodic and
cathodic, and with an anode and a cathode with the relevant supports as well as
the relative manufacturing procedure characterised by a simplification both of the
folding and/or moulding procedures and of the welding, and by a high quality
standard as regards the planarity of the finished bipolar plate and the absence of
defects capable of permitting the outflow of the process fluids to the external

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environment.
DESCRIPTION OF THE INVENTION
Under a first aspect, the invention consists of a bipolar plate comprising a single
wall provided with anodic and cathodic flanges, wherein the flanges are formed by
a preassembled frame provided with a suitable abutment surface for the single
wall directed to facilitate the execution of the perimetrical fixing weld between
frame and single wall.
In one embodiment of the invention, the preassembled frame has a U-profile and
is obtained by moulding or folding of a suitable strip of the same material as that
of the single wall.
In one alternative embodiment, the preassembled frame has a quadrangular
section and is obtained by draft of a draw piece of the same material as that of the
single wall.
In one preferred embodiment the perimetrical welding is carried out employing the
diode-laser technique.
In one preferred embodiment only one of the two faces of the bipolar plate single
wall is provided with longitudinal projections provided with an apex obtained by
moulding, wherein said projections are aligned in parallel to one of the sides of the
single wall itself.
In one preferred embodiment the bipolar plate comprises a first electrode or
current distributor and a second electrode or current distributor respectively
secured to the apexes of the projections and to strip-shaped supports positioned
on the face of the single wall free of projections; the strip-shaped supports are
optionally positioned in the recesses of the projections with their foot in
correspondence of the apex intrados.
In one preferred embodiment of the invention the first electrode or current
distributor, the apexes of the projections and the feet of the strip-shaped supports
are connected by means of a first single series of fixing welds.
In one preferred embodiment of the invention the second electrode or current
distributor is connected to the free terminal surfaces of the strip-shaped supports
by means of a second single series of fixing welds.

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In one further embodiment the apex of the projections is characterised by a planar
surface of reduced size.
Under another aspect, the invention relates to an electrolyser or fuel cell stack
comprising two compartments divided by a separator, optionally an ion-exchange
membrane or porous diaphragm, wherein each cell is delimited by bipolar plates
comprising a single wall and perimetrical flanges comprising a preassembled
frame provided with planar abutment surface for the welding to the single wall.
Under a final aspect the invention relates to a manufacturing method of bipolar
plates for electrolysers or fuel cells, comprising a single wall and perimetrical
flanges comprising a preassembled frame provided with planar abutment surface
for the welding to the single wall. In one preferred embodiment, the method
comprises the steps of folding or moulding of a sheet strip and of forming a U-
profiled frame with a planar abutment surface, or alternatively of extruding
quadrangular elements to form a frame with closed quadrangular profile and with
planar abutment surface; preassembling strip-shaped supports; moulding of
projections on just one side of the wall; positioning the perimetrical edge of the
single wall on the planar abutment surface of the frame and welding with diode-
laser technique; optional positioning of devices for biphasic fluid circulation on
said single wall and fixing by electric resistance welding, electric arc-welding or
laser welding; housing of the preassembled supports in the recesses of the
projections of the welded frame-single wall element, with positioning of the first
electrode or current distributor in contact with the apex of said projections and
execution of a single first series of welds by electric arc or laser-welding
technique; positioning of the second electrode or current distributor in contact with
the apex of said projections and execution of a single second series of welds by
electric arc or laser-welding technique.
DESCRIPTION OF THE DRAWINGS
Figure 1 sketches a portion of a cross-section of single wall bipolar plate
according to one of the embodiments of the prior art, wherein the two perimetrical
flanges are respectively obtained by folding or moulding of the single wall and by
welding of a preassembled element by folding or moulding of a suitable strip.

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Figure 2A shows a portion of a cross-section of a first embodiment of single wall
bipolar plate of the present invention, wherein the two flanges consist of a single
element preassembled in form of U-profiled perimetrical frame, where the frame,
formed by folding or moulding of a suitable strip, comprises an abutment surface
to facilitate the welding to the single wall.
Figure 2B shows a section of the perimetrical frame-single wall assembly resulting
from the welding of the elements of figure 2A.
Figure 2C illustrates a portion of a cross-section of single wall bipolar plate
according to a further embodiment of the invention, wherein the two flanges
consist of a single preassembled element in form of closed perimetrical frame with
quadrangular profile, where the closed frame presents an abutment surface for
the welding to the single wall.
Figure 3A represents a front-view of a possible embodiment of the single wall
provided with longitudinal projections on one side only.
Figure 3B shows the side section of the single wall of figure 3A along the line X -
X.
Figure 4A sketches a front-view of the assembly resulting from the welding of the
frame of figure 2A with the single wall of figure 3A according to the manufacturing
scheme of figure 2B.
Figure 4B illustrates the side section of the assembly of figure 4A along the line Y
-Y.
Figure 5 shows a side section of the assembly of figures 4A and 4B further
provided with the first electrode or current distributor on the side of the projection
apexes and of supports on the opposite side, wherein the first electrode or current
distributor, the apexes and the feet of the supports are fixed with a single first
series of welds.
Figure 6 reproduces in a three-dimensional scheme a detail of the assembly of
figure 5 with a side-view of the support, opposite to the side provided with first
electrode or current distributor.
Figure 7 finally represents the single wall bipolar plate resulting from the
completion of the assembly of figure 5 with the second electrode or current


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distributor fixed to the free terminal surfaces of the supports by a second single
series of welds.
DETAILED DESCRIPTION OF THE INVENTION
Figure 1 sketches the type of design proposed by the prior art for the construction
of a single wall-bipolar plate. In particular, the first flange (1a) is obtained by
folding or moulding of the single wall (1) itself, while the second flange (2) is
prepared separately as folded or moulded preassembled element making use of a
suitable strip: the preassembled element is then welded to the single wall through
the perimetrical weld (3) which involves the whole thickness of the two sheets (1)
and (2). The so obtained frame is finally completed with a reinforcing bar (4) of
metallic material, also carbon steel for instance, or of plastic material, such as for
example fibreglass-reinforced vinyl polyester. The problem characterising this
type of design derives from the presence of defects inside the weld (3): such
defects may put in communication the two process fluids present in operation on
the two sides of the bipolar plate, or one of the process fluids with the external
environment. While the former type of defect is tolerable within certain limits, the
latter type represents an utterly unfavourable occurrence. Of course, as known to
the experts in the field, the welds may be checked according to several methods
to identify the presence of defects capable of putting the interior of any chemical
apparatus or part thereof in communication with the external environment. Such
methods however slow down the production rates to a remarkable extent and
finally determine a substantial increase in the production costs.
Figures 2A, 2B and 2C sketch the solution to the problem of weld defects
proposed by the present invention. In particular, the two flanges are formed by a
single U-profiled frame-shaped element (5) which acts as barrier against the
external environment for the process fluids, as it consists of a continuous sheet.
This barrier action might be cancelled by defects contained in the weld (7) joining
the frame (5) to the single wall (1): to prevent the problem, the joining weld (7) is
executed by diode-laser technique. Such a procedure is characterised by the
possibility of predetermining the penetration of the fusion with high precision, even
in the case of the sheets making up the assembly, characterised by thicknesses

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indicatively comprised between a few tenths of a millimetre and 2 millimetres: with
a suitable adjustment, a weld bead (7) only partially penetrating the thickness of
the frame sheet (5) is obtained, so that the latter is preserved as an effective
barrier. Possible defects may only put in communication the process fluids
present on the two sides of the bipolar plate: this presence cannot be excluded
being inherent to the fusion welding process in itself, nevertheless it can be
minimised by further adjusting the welding parameters so as to obtain a broad
weld bead whose complete crossing by defects turns out to be substantially
unlikely. In order to guarantee the preservation of these very favourable
characteristics, the welding execution is facilitated by the peculiar profile of the
frame (5) which in fact presents a planar abutment surface (6) directed to realise a
regular contact with the peripheral edge of the single wall (1). In conclusion, the
adoption of the frame design and of the welding procedures of the invention
practically allows getting rid of the quality check procedures with a substantial
saving in the production costs.
It is to be noted that the employment of the diode laser welding technique would
not be decisive in the case of the frame according to the prior art design of figure
1: in fact while it is true that the welding parameters may be adjusted so as to
avoid the complete fusion of the sheet (1), thereby ensuring the separation of the
two process fluids present on the two sides of the single wall, it is also true that
the presence of possible defects contained, as mentioned before, in the weld
bead cannot be excluded. Such defects, if they are of sufficient size, would put the
process fluid present on the flange (2) side in contact with the external
environment. It follows that in any case, even with the adoption of a specialised
welding technique such as the laser-diode one, the prior art designs, of which the
one of figure 1 is an example, would anyway require the implementation of the
complex and expensive quality checks.
Figure 2C finally sketches a further embodiment of the invention wherein the two
flanges are again integrated in a single element, which however has the shape of
a closed frame (8) characterised by a quadrangular profile and including again the
planar abutment surface (6). In this particular embodiment, which can be obtained

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by continuous extrusion of quadrangular elements, the frame does not contain the
reinforcing bar (4), and the required mechanical resistance to compression is
ensured by a suitable thickness of the material. The hollow frame may be
employed as a duct for feeding the reactants through suitable feed nozzles and
suitable holes not shown in the figures.
In conclusion, the frame of the invention and the welding procedure with diode-
laser technique allows reducing the manufacturing costs in a significant way
because the leak checks to be carried out on the finished bipolar plates are
practically eliminated and nonetheless the bipolar plates assembled in the
electrolysers or stacks turn out to be practically free from defects capable of
putting the process fluids in communication with the external environment.
To avoid cancelling the advantage deriving from the cost reduction of the frame-
single wall assemblage it is necessary that also the costs of the subsequent
assembling operations of the electrode supports and of the first and second
electrode or current distributor be also limited.
A way to obtain this result is disclosed in the previously cited patent application
WO 03/038154 wherein the bipolar plate single wall is provided with projections
on both sides by moulding: the projections act as supports whereon the first and
second electrode or current distributor are subsequently secured. In this way only
two series of welds are employed in correspondence of the apexes of the
projections present on the two sides of the single wall. The procedure of WO
03/038154, which also allows some advantages associated to the internal
circulation of the process fluids, presents however a drawback which is difficult to
overcome in the practice: the single wall, subjected to the double moulding
necessary to obtain the projections on both sides, undergoes deep irreversible
distortions with consequent lack of planarity and mechanical tears, which jointly
cause a high percentage of rejections with a consequent critical burdening of the
production costs.
On the other hand as mentioned the conventional technique, sketched in figure 7
of EP 1 366 212, effectively allows obtaining highly planar bipolar plates by
employing strip-shaped supports whose fixing to the single wall jointly with the first

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and second electrode or current distributor however requires carrying out four
series of welds: it is clear therefore that the assembled elements are
characterised by high quality but at the expense of the costs of production which
undoubtedly turn out to be remarkable.
The present invention achieves the scope of having bipolar plates of high planarity
while keeping the production costs within reasonable and market-acceptable limits
resorting to a hybridisation of the previously disclosed technologies.
Figure 3 shows that the single wall (1) is provided with projections (9) on one side
only: the moulding procedure is hence simplified with very reduced mechanical
stresses. It follows that the deformations of the single wall after moulding are
minimal and, if desired, easily eliminable by press rectification.
Figures 4A and 4B sketch how the single wall (1) is then positioned on the
abutment surface (6) of the perimetrical frame (5), optionally provided with a
reinforcing bar (4), to be fixed by means of the weld (7).
Figure 5 summarises the subsequent manufacturing step, in which the assembly
of frame (5) and single wall (1) provided with projections (9) on one side only is
equipped with a first electrode or current distributor (10) in contact with the apexes
of the projections (9) and, on the side opposite the projections, with supports (11)
in form of strips housed in the recesses of the projections: the mutual fixing of the
three components (first electrode or current distributor (10), apexes of the
projections (9) and supports (11)) is carried out through a single series of welds
schematically indicated as (12). The best result in terms of mechanical stiffness,
electric current conduction in operation and absence or in any case minimum
number of defects is obtained making use of the laser welding technique for
instance with a carbon dioxide-laser whose high fusion penetration allows
securing the above seen components simultaneously. The supports (11) are
positioned inside the projections (9) in contact with the apex intrados, which
presents a planar portion to favour the contact with the foot of the same supports.
The developing of the planar surface of the projection (9) apexes is limited to what
required to achieve a good bearing seat for the support feet, in order to avoid that,
during operation, the electrode or distributor (10) become the site for shielding

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phenomena, which are hazardous in particular for the integrity of the ion-
exchange membranes, if they are in contact with the first electrode fixed to the
projections, or for the reaction gas diffusion, if gas diffusion electrodes are
employed, in this case positioned on the first current distributor fixed to the
projections. The supports (9) consist of sheet strips with a thickness indicatively
comprised between 1 and 5 millimetres. The optimal thickness of the supports
strips is the result of a compromise between the two needs of conducting the
electric current in the best possible fashion (high thicknesses) and of preventing
the same shielding zone-formation phenomenon seen in the case of the first
electrode or current distributor, in correspondence of the junction areas with the
second electrode or current distributor (low thicknesses).
In figures 4 and 5 a preferred embodiment of the invention is represented,
wherein the projections (9) have a prismatic shape with slightly lower length than
the single wall, so as to facilitate the positioning of the supports (11) inside the
same projections. It is of course also possible to produce projections consisting of
aligned segments which have the merit of favouring the reaction fluid mixing in
operation: in this case, the supports are fractioned as well in segments of length
such that an easy housing of each segment inside each series of projections is
permitted.
Figure 6 shows a three-dimensional detail of the assembly of figure 5 (zone
delimited by a circle) with a view from the side of the supports opposite the side
wherein the first electrode or current distributor is in contact with the apexes of the
projections: (4) indicates the reinforcing bar, (5) the perimetrical frame moulded in
a single piece of strip, (16) the internal surface of projections (9), (11) the strip-
shaped support whose foot in contact with the planar portion (13) of the projection
apex is secured by the first series of welds (12).
In figure 7 it is shown the completion of the element of figure 5 with the attainment
of the bipolar plate in accordance with the invention: the second electrode or
current distributor (14) is put in contact with the free terminal surfaces of the
supports (11) and is secured by a single second series of welds (15), which may
be carried out by various procedures, for instance by electrical resistance, electric

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arc and preferably laser in consideration of the higher speed.
In order that the various types of weld seen above present the required quality it is
also necessary that the various components of the bipolar plate of the invention
be maintained in a precise contact condition during the whole time of
manufacturing. For this purpose the various components, frame and single wall
during the step of execution of the fixing weld (7), first electrode or current
distributor (10), single wall (1) fixed to the perimetrical frame (5) and supports (11)
during the step of execution of the first single series of welds (12), and finally
element obtained by means of the first single series of welds and second
electrode or current distributor (14), should be accurately blocked within a suitable
construction template.
As regards the dimensions of the bipolar plate of the invention, the height of the
projections and supports is selected in the simplest case so that the distance of
the two electrodes or current distributors from the single wall surface results the
same. This type of symmetrical design is employed for instance for the production
of bipolar plates directed to be assembled in electrolysers for the conventional
electrolysis of hydrochloric acid solutions and for the water electrolysis with
potassium hydroxide solutions: in these cases the construction materials for the
single wall provided with projections, for the supports and for the electrodes or
current distributors are respectively titanium or alloys thereof and nickel. In both
cases the solutions contain the product gases (respectively chlorine-hydrogen,
and oxygen-hydrogen) as bubble dispersion: to favour the circulation of the
biphasic fluids, a suitable depth of the anodic and cathodic compartments is
required and therefore the projections and supports are dimensioned so as to
achieve a surface distance of single wall - electrode or current distributor
indicatively comprised between 30 and 50 millimetres. Optionally, one or both of
the compartments, anodic and cathodic, may be equipped with devices directed to
further promote the biphasic fluid circulation and to accelerate the gas bubble
coalescence and the separation thereof from the liquid. Similar devices, such as
channel and planar flow deflectors installed in a suitable position on one or both
faces of the bipolar plate single wall, are for instance disclosed in WO 03/048420.

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The bipolar plate of the invention can be advantageously used also for
assembling electrolysers directed to the electrolysis of hydrochloric acid solutions
and equipped with oxygen diffusion cathodes wherein, much as in the case of the
conventional electrolysis, the construction material for the single wall provided
with projections, supports and electrodes or current distributors is titanium or
alloys thereof. The design can be modified in an interesting fashion: in fact if the
oxygen diffusion cathode is installed on the side of the single wall provided with
projections, the height of the latter is advantageously reduced since the process
fluid on this side is oxygen or air which, being a gaseous phase, requires an
entirely modest compartment width. It follows that the moulding operation is very
simplified and that the single wall, subjected to moderate deformations, turns out
being substantially planar without the need of subsequent straightening
interventions. In particular, the single wall - electrode or current distributor
distance is comprised between 5 and 10 millimetres. Moreover the moderate
moulding stresses eliminate completely the possibility of generating those tears
which are conversely a frequent event during the moulding of the projections of
WO 03/038154.
The other (anodic) side of the single wall is in contact with the hydrochloric acid
solution containing a dispersion of chlorine bubbles: the correct circulation of this
biphasic mixture requires that the compartment have an adequate depth and the
supports are therefore designed with a height such that it ensures an electrode
(anode) - single wall surface distance comprised between 30 and 50 millimetres
as seen above.
The bipolar plate of the invention is also usable for the construction of membrane
fuel cell assemblies (known as stacks). Since in this kind of cells the process
fluids are air on the cathode side and hydrogen or hydrogen-containing mixture on
the anode side, the depth of both compartments, only crossed by gaseous
phases, can be modest: it follows that the projections and likewise the supports
have reduced heights (with the above seen advantages), with a single wall -
electrode or current distributor distance even lower than 5 mm on both sides,
anodic and cathodic.

WO 2006/053768 PCT/EP2005/012381
16
In all the above disclosed applications of electrolysers or stacks comprising a
multiplicity of bipolar plates of the invention a deterioration of the electrodes or
current distributors, which must therefore be replaced with new components,
takes place after a certain operating time. In the case of the second electrode or
current distributor the replacement is carried out by eliminating the securing welds
to the supports, for instance by grinding, and by welding the new replacement
piece to the freed terminal surfaces of the supports. This procedure in general is
to be avoided for the first electrode or current distributor since the risks of
damaging the thin sheet of the projections is too high: a preferable alternative
procedure provides that a new electrode or current distributor, thinner than the
damaged one, be secured by welding, for instance by the cheap resistance spot-
welding. The first damaged electrode or current distributor, which is then left in
place, favours the homogeneous current distribution to the new thinner piece.
The structure of the bipolar plate of the invention and the relevant assembly
procedure of the various constituent elements justify the above given definition of
hybridisation: in fact, the bipolar plate structure of the invention makes use
advantageously of the projections moulded on the single wall and of the strip-
shaped supports of the prior art mutually combining the same in a novel fashion.
The disclosed combination allows assembling the components (first and second
electrode or current distributor, single wall with projections on one side only and
strip-shaped supports) with just two series of welds, obtaining the same
economical advantages of the welding process of WO 03/038154, while avoiding
to resort to excessively difficult moulding operations.
In the descriptions contained in the present text, reference has been made to
some preferred embodiments, nevertheless it is clear to those skilled in the art
that several modifications are possible without departing from the scope of the
invention, which is solely defined and limited by the following claims.

17
CLAIMS
1. Bipolar plate for electrochemical cells comprising a first and a second
compartment divided by a separator and respectively containing a first and a
second electrode or current distributor, said bipolar plate comprising a single wall.
perimetrical flanges and means for feeding reactants and extracting products, said
perimetrical flanges comprising a preassembled frame provided with a planar
abutment surface for the welding with said single wall, wherein said single wall is
provided with projections on one side only and of supports on the side opposite to
that of the projections.
2. The bipolar plate of claim 1 wherein said welding between said planar
abutment surface of the frame and said single wall is a diode laser welding.
3. The bipolar plate of claim 1 or 2 wherein said frame has a generally U-
shaped profile.
4. The bipolar plate of claim 1 or 2 wherein said frame has a quadrangular
closed profile.
5. The bipolar plate of any one of the preceding claims wherein said means for
feeding reactants consists of said preassembled frame, provided with a multiplicity
of distributing holes.
6. The bipolar plate of any one of the preceding claims wherein said
projections are longitudinal projections parallel to one side of the bipolar plate.
7. The bipolar plate of claim 6 wherein said projections are continuous
projections having a length slightly lower than the length of said side.
8. The bipolar plate of any one of claims 1 to 8 wherein said supports are
strips of sheet comprising a foot housed in the recesses of said projections.
9. The bipolar plate of any one of claims 1 to 9 wherein said first electrode or
current distributor is in contact with the apexes of said projections.
10. The bipolar plate of claim 9 wherein said first electrode or current
distributor, said projection apexes in contact therewith and the feet of said
supports are connected through a single first series of welds.
11. The bipolar plate of claim 10 wherein said single first series of welds
comprises electrical resistance welds or electric arc welds or laser welds.

18
12. The bipolar plate of any one of claims 1 to 11 wherein said second
electrode or current distributor is in contact with the free terminal surfaces of said
supports.
13. The bipolar plate of claim 12 wherein said second electrode or current
distributor and said free terminal surfaces of the supports are connected through a
single second series of welds.
14. The bipolar plate of claim 13 wherein said single second series of welds
comprises electrical resistance welds or electric arc welds or laser welds,
15. The bipolar plate of any one of claims 1 to 14 wherein said projections have
an apex provided with a planar surface of low width.
16. The bipolar plate of any one of the preceding claims wherein the distances
between said first and second electrode or current distributor and said single wall
are equal.
17. The bipolar plate of claim 16 wherein said distances are comprised between
5 and 50 millimetres.
18. The bipolar plate of any one of claims 1 a 16 wherein the distance between
said first electrode or current distributor and said single wall is lower than the
distance between said second electrode or current distributor and said single wall.
19. The bipolar plate of claim 18 wherein said distances are respectively
comprised between 5 and 50 millimetres and between 30 and 50 millimetres.
20. The bipolar plate of any one of the preceding claims wherein said single
wall is provided with devices for improving the circulation of biphasic fluids.
21. An electrolyser comprising a multiplicity of elementary cells comprising
bipolar plates of any one of the preceding claims.
22. The electrolyser of claim 21 wherein peripheral sealing gaskets and
separators are intercalated between adjacent pairs of said bipolar plates.
23. The electrolyser of claim 22 wherein said separators are ion-exchange
membranes or porous diaphragms.
24. A stack comprising a multiplicity of fuel cells comprising bipolar plates of
any one of claims from 1 to 20.
25. The stack of claim 24 wherein peripheral sealing gaskets and separators
are intercalated between adjacent pairs of said bipolar plates.

19
26. The stack of claim 25 wherein said separators are ion-exchange
membranes or porous diaphragms.
27, Method for the manufacturing of the bipolar plate of claim 14 or 15
comprising the steps of:
- folding or moulding of a sheet strip to form said frame with U-shaped profile and
with planar abutment surface or by drafting of quadrangular elements to form said
frame with closed quadrangular profile and with planar abutment surface
- preassembly of said strip-shaped supports
- moulding of said projections on one side only of said single wall
- positioning of the perimetrical edge of said single wall on the planar abutment
surface of said frame and welding with diode laser technique
- optional positioning of devices for improving the circulation of biphasic fluids on
said single wait and fixing by electric resistance welding, or electric arc welding or
laser welding
- housing of said preassembled supports in the recesses of said projections of the
welded frame - single wall element, positioning of said first electrode or current
distributor in contact with the apex of said projections and execution of said first
single series of welds by electric arc welding or laser welding technique
- positioning of said second electrode or current distributor in contact with the free
terminal surfaces of said supports and execution of said second single series of
welds by electric resistance welding or electric arc welding or laser welding
technique.

It is described a bipolar plate consisting of a single wall and a perimetrical sealing frame
obtained by folding and provided with a planar abutment surface for the frame-to-wall
welding. The wall in further provided with projections on one face thereof preferably
obtained by moulding and with supports on the other face consisting of sheet strips
housed in the recesses formed by the concave part of the projections. The projections
substantially extend along the entire length of the bipolar plate. The projections and
supports are connected to electrodes or current distributors. The projections, the
supports, the single wall and the perimetrical frame are made of the same metal or
alloy. The electrode or current distributor supported by the projections, the same
projections and the supports are welded together by a single pass of are-welding or
preferably laser-welding. The electrode or current distributor connected to the support
and the support themselves are mutually welded by a subsequent pass of the welding
or preferably laser-welding. The welding between wall and perimetrical frame on the
abutment surface of the frame is carrier out by diode-laser technique, allowing to
obtain a robust connection but without a complete melting of the sheet, thereby
eliminating the risk of process fluid leakage to the external environment.

Documents:

01828-kolnp-2007-abstract.pdf

01828-kolnp-2007-claims.pdf

01828-kolnp-2007-correspondence others 1.1.pdf

01828-kolnp-2007-correspondence others 1.2.pdf

01828-kolnp-2007-correspondence others 1.3.pdf

01828-kolnp-2007-correspondence others 1.4.pdf

01828-kolnp-2007-correspondence others.pdf

01828-kolnp-2007-description complete.pdf

01828-kolnp-2007-drawings.pdf

01828-kolnp-2007-form 1.pdf

01828-kolnp-2007-form 2.pdf

01828-kolnp-2007-form 3.pdf

01828-kolnp-2007-form 5.pdf

01828-kolnp-2007-gpa.pdf

01828-kolnp-2007-international publication.pdf

01828-kolnp-2007-international search report.pdf

01828-kolnp-2007-other pct form.pdf

01828-kolnp-2007-pct request form 1.1.pdf

01828-kolnp-2007-pct request form.pdf

01828-kolnp-2007-priority document 1.1.pdf

01828-kolnp-2007-priority document.pdf

1828-KOLNP-2007-(05-07-2013)-CORRESPONDENCE.pdf

1828-KOLNP-2007-(18-07-2014)-ANNEXURE TO FORM 3.pdf

1828-KOLNP-2007-(18-07-2014)-CLAIMS.pdf

1828-KOLNP-2007-(18-07-2014)-CORRESPONDENCE.pdf

1828-KOLNP-2007-(18-07-2014)-DESCRIPTION (COMPLETE).pdf

1828-KOLNP-2007-(18-07-2014)-DRAWINGS.pdf

1828-KOLNP-2007-(18-07-2014)-FORM-1.pdf

1828-KOLNP-2007-(18-07-2014)-FORM-2.pdf

1828-KOLNP-2007-(18-07-2014)-OTHERS.pdf

1828-KOLNP-2007-(18-07-2014)-PETITION UNDER RULE 137.pdf

1828-kolnp-2007-form 18.pdf

abstract-01828-kolnp-2007.jpg


Patent Number 263939
Indian Patent Application Number 1828/KOLNP/2007
PG Journal Number 49/2014
Publication Date 05-Dec-2014
Grant Date 27-Nov-2014
Date of Filing 23-May-2007
Name of Patentee UHDENORA S.P.A.
Applicant Address VIA BISTOLFI, 35 20134 MILAN
Inventors:
# Inventor's Name Inventor's Address
1 FULVIO, FEDERICO VIA SCALABRINI, 4 I-29100 PIACENZA
2 OLDANI, DARIO VIA PAOLO SARPI, 44 I-20154 MILAN
3 MOJANA, CORRADO VIA CAMPOGRANDE, 66 I-23868 VALMADRERA(LC)
4 CARRETTIN, LEONELLO VIA SODERINI, 55, I-20146 MILAN
PCT International Classification Number C25C 7/00, C25B 11/00
PCT International Application Number PCT/EP2005/012381
PCT International Filing date 2005-11-18
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 MI2004A002248 2004-11-19 Italy