Technical Field
[0001] The present invention relates to a bipolar plate for use in a PEM electrolysis device.
The present invention further relates to a PEM electrolysis device having at least
one such bipolar plate.
Background
[0002] A PEM electrolysis device (PEM = proton exchange membrane) is used for the acidic
electrolysis of water into oxygen and hydrogen. The anode and cathode are separated
from each other by a proton conducting membrane. A bipolar plate provided as a battery
separator in the PEM electrolysis device separates the anode space and the cathode
space of the PEM electrolysis device from each other. The bipolar plate on the cathode
side is usually composed of titanium plates. Titanium in the PEM electrolysis device
can add hydrogen and thus cause hydrogen embrittlement, which reduces the operating
time of the bipolar plate and thereby the operating time of the electrolysis device.
Hydrogen embrittlement can be reduced by coating at least the hydrogen-exposed cathode
side of the bipolar plate with carbon.
[0003] A bipolar plate for an electrochemical battery is known, for example, from
DE 10 2014 109 321 A1. The bipolar plate comprises a substrate having a substrate surface and a coating
applied to at least a portion of the substrate surface. The coating comprises a rough
and/or porous covering layer which is applied to the substrate surface in a plasma
metal spraying process and has a rough and/or porous covering layer surface pointing
away from the substrate. The coating also comprises a protective layer, wherein the
covering layer surface is provided or covered with the protective layer. The substrate
is configured with a flat plate shape and is made of steel, in particular stainless
steel, copper and/or aluminum.
[0004] Furthermore,
DE 10 2013 207 082 A1 discloses a PEM electrolysis device comprising a battery separator with a steel/titanium
bimetallic plate.
Summary
[0005] The objective of the present invention is to provide an alternative bipolar plate
for use in a PEM electrolysis device and an alternative PEM electrolysis device. In
particular, the bipolar plate can be produced cost-effectively and has high corrosion
resistance as well as high oxidation resistance. In addition, the PEM electrolysis
device can also have higher efficiency and longer service life.
[0006] The objective is achieved by the bipolar plate having the feature of Claim 1 and
by the PEM electrolysis device having the feature of Claim 10. Preferred or advantageous
embodiments of the present invention are derived from the dependent claims and the
following description and drawings.
[0007] A bipolar plate for use in a PEM electrolysis device according to the present invention
is composed of at least one polymer material, and has a cathode side comprising carbon
filling particles and an anode side comprising metal particles, metal carbide particles
and/or metal nitride particles. In other words, the bipolar plate is configured in
a multiple-layer manner, wherein at least two layers are provided with different functions
and/or properties. In particular, the bipolar plate is composed of at least one composite
material. The layer forming the cathode side and the layer forming the anode side
are inseparably connected to one another, in particular via positive locking and/or
material connection. For example, the cathode side and the anode side of the bipolar
plate are connected to each other indirectly via another layer or another element,
or immediately adjacent, i.e., directly inseparably connected to one another.
[0008] For example, polymer mixtures composed of at least one polymer and carbon filling
particles and of at least one polymer material and metal particles, metal carbide
particles and/or metal nitride particles can be injection molded, in particularly
by injection molding or pressure casting, into the bipolar plate. Alternatively, polymer
mixtures composed of at least one polymer and carbon filling particles and of at least
one polymer material and metal particles, metal carbide particles and/or metal nitride
particles can be pressed, in particular by rolling, deformation, molding, into the
bipolar plate. In particular, it is also possible to combine these methods with one
another, so that the bipolar plate is first injection molded and then pressed.
[0009] According to a preferred embodiment of the present invention, the metal particles,
metal carbide particles and metal nitride particles are selected from titanium, niobium,
silver, gold, platinum, iridium, titanium carbide, niobium carbide, titanium nitride
and niobium nitride. As an alternative or supplement to this, using metered or unmetered
tin oxide on the anode side can also be envisaged. In particular, metal particles,
metal carbide particles and metal nitride particles are oxidation-resistant and have
higher oxidation resistance than carbon filling particles.
[0010] According to a preferred embodiment of the present invention, the carbon filling
particles are selected from carbon black, graphite, graphene, carbon fibers and carbon
nanotubes. In particular, the carbon filling particles are electrically conductive.
Preferably, the content of carbon filling particles in at least one polymer material
on the cathode side is at least 70 vol.%. For example, the content of carbon filling
particles in polymer materials can be determined by X-ray structural analysis (XRD).
vol.% is an abbreviation for volume percent.
[0011] According to a preferred embodiment of the present invention, the bipolar plate is
composed at least partly or completely of at least one thermoplastic selected from
PP (polypropylene), PVF (polyvinyl fluoride), PVDF (polyvinylidene fluoride), PTFE
(polytetrafluoroethylene), PCTFE (polychlorotrifluoroethylene), ETFE (ethylene-tetrafluoroethylene
fluorine copolymer), PA (polyamide), PPA (polyphthalamide), PPS (polyphenylene sulfide),
LCP (liquid crystal polymer), PEEK (polyetheretherketone), PC (polycarbonate), PSU
(polysulfone), PESU (polyethersulfone), and PEI (polyetherimide). In other words,
the bipolar plate may be composed of at least one of the aforementioned thermoplastics
or of a combination of at least two or more thermoplastics.
[0012] According to a preferred embodiment of the present invention, the bipolar plate is
composed at least partly or completely of at least one thermosetting plastic selected
from phenolic resins, epoxy resins, melamine resins, unsaturated polyester resins,
polyimides and polyamide-imides. In other words, the bipolar plate may be composed
of at least one of the aforementioned thermosetting plastics or of a combination of
at least two or more thermosetting plastics.
[0013] According to a preferred embodiment of the present invention, the bipolar plate is
composed at least partly or completely of at least one elastomer selected from FKM
(fluororubber), FFKM (perfluororubber), EPDM (ethylene-propylene-diene rubber), CR
(neoprene rubber), IIR (isobutylene-isoprene rubber), CSM (chlorosulfonyl-polyethylene
rubber), FVMQ (fluorosilicone rubber). In other words, the bipolar plate may be composed
of at least one of the aforementioned elastomers or of a combination of at least two
or more elastomers. For example, the bipolar plate may be composed of a combination
of two or more of the thermoplastics, thermosetting plastics, and elastomers described
above.
[0014] According to a preferred embodiment of the present invention, a reinforcer is arranged
at least partially or completely between the cathode side and the anode side. The
reinforcer is used in particular to increase the rigidity of the bipolar plate. In
other words, the bipolar plate has at least three layers, namely a layer forming the
cathode side, a layer forming the anode side and a layer forming the reinforcer. All
three layers are inseparably connected to one another, in particular via positive
locking and/or material connection. Preferably, the reinforcer is configured as a
metal mesh or a metal strip. For example, the metal mesh or metal strip is composed
at least partially or completely of steel including a corrosion-resistant coating,
stainless steel, especially a high-grade steel, copper, especially a copper alloy,
and/or aluminum, especially an aluminum alloy. The surface of the metal mesh or metal
strip is preferably rough and/or structured in order to be better attached to the
at least one polymer material of the anode side and/or cathode side. Roughness or
structures are produced on the surface of the metal mesh or metal strip, in particular
by rolling, deformation, sandblasting and/or by means of laser processing.
[0015] If no reinforcer is used between the cathode side and the anode side, a resin packaging
portion for reducing the gas diffusivity of the bipolar plate may be used between
the cathode side and the anode side.
[0016] During the production of the bipolar plate by rolling, in particular during the production
of composite materials or during the production of reinforcers, at least one roller
can be heated and at least one roller can be cooled. The temperature influence during
rolling can have a favorable effect on the properties of the bipolar plate, in particular
on the structure and distribution of filling particles and metal elements in the polymer
material.
[0017] A PEM electrolysis device according to the present invention comprises at least one
bipolar plate according to the present invention. For example, the bipolar plate is
provided as a battery separator in the PEM electrolysis device.
Brief Description of the Drawings
[0018] The improvement measures of the present invention will be described in detail below
in combination with the accompanying drawings and the description of the preferred
embodiments of the present invention. Shown here:
FIG. 1 shows a schematic view of a PEM electrolysis device having a bipolar plate
configured as a battery separator according to a first embodiment, according to embodiments
of the present invention,
FIG. 2 shows a schematic view of the bipolar plate in FIG. 1, and
FIG. 3 shows a schematic view of the bipolar plate according to a second embodiment.
Detailed Description
[0019] FIG. 1 shows a PEM electrolysis device 2 having two batteries 6.1 and 6.2 and a bipolar
plate 1 arranged as a battery separator between the two batteries 6.1 and 6.2. In
particular, the PEM electrolysis device 2 can comprise additional batteries, which
are connected, for example, on both sides, wherein the batteries are separated from
one another by the respective bipolar plate. The bipolar plate 1 is here configured
in a two-layer manner and comprises a cathode side 3 and an anode side 4, wherein
the cathode side 3 is composed of a first composite material and the anode side 4
is composed of a second composite material.
[0020] The first composite material is composed of a polymer having carbon filling particles.
The second composite material is composed of a polymer having metal particles. Furthermore,
as an alternative or supplement to metal particles, metal carbide particles and/or
metal nitride particles may in particular be provided in the second polymer. In particular,
the carbon filling particles are electrically conductive, and the metal particles
are oxidation-resistant.
[0021] A porous transport layer 7.1 first adjoins on the cathode side 3 of the bipolar plate
1, while a catalytic layer 8.1 is arranged on the transport side and a membrane 9.1
is arranged on the catalytic layer. The cathode side 3 of the bipolar plate 1 forms
a cathode 10 together with the adjacent porous transport layer 7.1 and the catalytic
layer 8.1. Arranged adjacent to the other side of the membrane 9.1 is a catalytic
layer 8.2, on which is arranged a porous transport layer 7.2 and an anode side 14
of a further bipolar plate, not shown in detail, on the transport layer. The anode
side 14 of the bipolar plate, not shown in detail, forms an anode 11 together with
the adjacent porous transport layer 7.2 and the catalytic layer 8.2. The battery 6.1
extends from the anode side 14 of the bipolar plate, not shown in detail, to the cathode
side 3 of the bipolar plate 1.
[0022] A porous transport layer 7.3 first adjoins on the anode side 4 of the bipolar plate
1, while a catalytic layer 8.3 is arranged on the transport side and a membrane 9.2
is arranged on the catalytic layer. The anode side 4 of the bipolar plate 1 forms
an anode 12 together with the adjacent porous transport layer 7.3 and the catalytic
layer 8.3. Arranged adjacent to the other side of the membrane 9.2 is a catalytic
layer 8.4, on which is arranged a porous transport layer 7.4 and a cathode side 15
of a further bipolar plate, not shown in detail, on the transport layer. The cathode
side 15 of the bipolar plate, not shown in detail, forms a cathode 13 together with
the adjacent porous transport layer 7.4 and the catalytic layer 8.4. The battery 6.2
extends from the cathode side 15 of the bipolar plate, not shown in detail, to the
anode side 4 of the bipolar plate 1.
[0023] The function of the PEM electrolysis device 1 and its individual components for the
production of hydrogen and oxygen from water is known in the prior art and will not
be described in detail here.
[0024] FIG. 2 shows a two-layer bipolar plate 1 according to FIG. 1. The cathode side 3
can be composed of thermoplastics, thermosetting plastics and/or elastomers, which
has metal particles, metal carbide particles and/or metal nitride particles. The particles
are composed in particular of titanium, niobium, silver, gold, platinum, iridium,
titanium carbide, niobium carbide, titanium nitride and/or niobium nitride. The anode
side 4 can be composed of thermoplastics, thermosetting plastics and/or elastomers,
which has carbon filling particles. The carbon filling particles are composed in particular
of carbon black, graphite, graphene, carbon fibers and/or carbon nanotubes, wherein
the content of the carbon filling particles in the polymer material of the anode side
4 is at least 70 vol.%. The cathode side 3 and the anode side 4 are connected to one
another via material connection. Since the bipolar plate 1 is shown in a simplified
manner, the outwardly facing surface is not shown in a structured manner, although
the outwardly facing surface may have structures, in particular recesses and protrusions,
through which at least the water for electrolysis is supplied and guided.
[0025] FIG. 3 shows a three-layer bipolar plate 1 according to a second embodiment. In this
case, a reinforcer 5 configured as a metal mesh or a metal strip is arranged between
the cathode side 3 and the anode side 4. The cathode side 3 and the reinforcer 5 are
connected to one another via material connection like the anode side 4 and the reinforcer
5. The three-layer bipolar plate 1 according to FIG. 3 otherwise corresponds to the
two-layer bipolar plate 1 according to FIGs. 1 and 2.
LIST OF REFERENCE NUMERALS
[0026]
- 1
- Bipolar plate
- 2
- PEM electrolysis device
- 3
- Cathode side of the bipolar plate
- 4
- Anode side of the bipolar plate
- 5
- Reinforcer
- 6.1
- Battery
- 6.2
- Battery
- 7.1
- Transport layer
- 7.2
- Transport layer
- 8.1
- Catalytic layer
- 8.2
- Catalytic layer
- 9.1
- Membrane
- 9.2
- Membrane
- 10
- Cathode
- 11
- Anode
- 12
- Anode
- 13
- Cathode
- 14
- Anode side
- 15
- Cathode side
1. A bipolar plate (1) for use in a PEM electrolysis device (3), wherein the bipolar
plate (1) is composed of at least one polymer material, and has a cathode side (3)
comprising carbon filling particles and an anode side (4) comprising metal particles,
metal carbide particles and/or metal nitride particles.
2. The bipolar plate (1) according to Claim 1, characterized in that the metal particles, metal carbide particles and metal nitride particles are selected
from titanium, niobium, silver, gold, platinum, iridium, titanium carbide, niobium
carbide, titanium nitride and niobium nitride.
3. The bipolar plate (1) according to Claim 1 or 2, characterized in that the carbon filling particles are selected from carbon black, graphite, graphene,
carbon fibers and carbon nanotubes.
4. The bipolar plate (1) according to any one of the preceding claims, characterized in that the content of the carbon filling particles in the at least one polymer material
is at least 70 vol.%.
5. The bipolar plate (1) according to any one of the preceding claims, characterized in that the bipolar plate (1) is composed at least partially of at least one thermoplastic
selected from PP, PVF, PVDF, PTFE, PCTFE, ETFE, PA, PPA, PPS, LCP, PEEK, PC, PSU,
PESU and PEI.
6. The bipolar plate (1) according to any one of the preceding claims, characterized in that the bipolar plate (1) is composed at least partially of at least one thermosetting
plastic selected from phenolic resins, epoxy resins, melamine resins, unsaturated
polyester resins, polyimides and polyamide-imides.
7. The bipolar plate (1) according to any one of the preceding claims, characterized in that the bipolar plate (1) is composed at least partially of at least one elastomer selected
from FKM, FFKM, EPDM, CR, IIR, CSM, FVMQ.
8. The bipolar plate (1) according to any one of the preceding claims, characterized in that a reinforcer (5) is at least partially arranged between the cathode side (3) and
the anode side (4).
9. The bipolar plate (1) according to Claim 8, characterized in that the reinforcer (5) is configured as a metal mesh or a metal strip.
10. A PEM electrolysis device (2) comprising the bipolar plate (1) according to any one
of the preceding claims.