Gas diffusion layer, electrochemical cell having such a gas diffusion layer, and electrolyzer
10294572 ยท 2019-05-21
Assignee
Inventors
Cpc classification
C25B9/23
CHEMISTRY; METALLURGY
Y02E60/50
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
Y02E60/36
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
Abstract
A gas diffusion layer is arranged between a bipolar plate and an electrode of an electrochemical cell and includes at least two layers which are layered one on top of the other layer. At least one of the two layers is designed as a spring component having a progressive spring characteristic curve.
Claims
1. A gas diffusion layer arranged between a bipolar plate and an electrode of an electrochemical cell, said gas diffusion layer comprising: at least two separate layers formed as elements which are separate from each other, with one of the separate layers being layered on top of another one of the separate layers; and a spring component forming at least one of the at least two separate layers, said spring component having a progressive spring characteristic curve selected so as to achieve a deformation in a range of a normal contact pressure of 5-25 bars.
2. The gas diffusion layer of claim 1, wherein the gas diffusion layer has at least three separate layers formed as elements which are separate from each other and being layered on top of each other, said spring component forming an outer separate layer of the gas diffusion layer.
3. The gas diffusion layer of claim 1, wherein the at least two separate layers have different structure and/or composition.
4. The gas diffusion layer of claim 1, wherein the gas diffusion layer has at three layers, a first one of the layers configured as a contacting component, a second one of the layers configured as a diffusion component, and a third one of the layers configured as the spring component.
5. The gas diffusion layer of claim 1, wherein the spring characteristic curve of the spring component is divided into at least two regions of differing progression.
6. The gas diffusion layer of claim 1, wherein the spring characteristic curve of the spring component is divided into at least three regions of differing progression.
7. The gas diffusion layer of claim 1, wherein the spring component is deformed up to 60% of a maximum elastic deformation when a contact pressure of up to 5 bar is applied.
8. The gas diffusion layer of claim 1, wherein the spring component is deformed up to 80% of a maximum elastic deformation when a contact pressure of up to 5 bar is applied.
9. The gas diffusion layer of claim 1, wherein the spring component is deformed between 60% to 90% of a maximum elastic deformation when a contact pressure between 5 bar and 25 bar is applied.
10. The gas diffusion layer of claim 1, wherein the spring component is formed from an electrically conductive material.
11. The gas diffusion layer of claim 10, wherein the electrically conductive material is selected from the group consisting of steel, titanium, niobium, tantalum, nickel, and any combination thereof.
12. The gas diffusion layer of claim 1, wherein the spring component is formed as a profiled metal sheet.
13. The gas diffusion layer of claim 1, wherein the spring component is formed as a mesh.
14. The gas diffusion layer of claim 1, wherein the spring component comprises one or more spirals.
15. An electrochemical cell, comprising: a bipolar plate; an electrode; and a gas diffusion layer arranged between the bipolar plate and the electrode, said gas diffusion layer including at least two separate layers formed as elements which are separate from each other, with one of the layers being layered on top of another one of the layers, and a spring component forming at least one of the at least two separate layers, said spring component having a progressive spring characteristic curve selected so as to achieve a deformation in a range of a normal contact pressure of 5-25 bars.
16. The electrochemical cell of claim 14 constructed as a PEM electrolysis cell or a galvanic cell.
17. An electrolyzer, comprising a PEM electrolysis cell which includes a bipolar plate, an electrode, and a gas diffusion layer arranged between the bipolar plate and the electrode, said gas diffusion layer including at least two separate layers formed as elements which are separate from each other, with one of the layers being layered on top of another one of the layers, and a spring component forming at least one of the at least two layers, said spring component having a progressive spring characteristic curve selected so as to achieve a deformation in a range of a normal contact pressure of 5-25 bars.
Description
BRIEF DESCRIPTION OF THE DRAWING
(1) Exemplary embodiments of the invention can be explained with reference to a drawing, in which:
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(11) Identical reference signs have the same meaning in the various figures.
DETAILED DESCRIPTION OF THE EMBODIMENTS
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(13) The electrochemical cell 2 comprises an electrolyte consisting of a proton-conducting membrane 4 (Proton-Exchange-Membrane, PEM), on both sides of which are located the electrodes 6a, 6b. The assembly consisting of membrane and electrodes is referred to as a membrane-electrode-assembly (MEA). 6a in this respect denotes a cathode, and 6b denotes an anode. A gas diffusion layer 8 rests in each case on the electrodes 6a, 6b. The gas diffusion layers 8 are contacted by what are termed bipolar plates 10, which in the assembled state of an electrolysis stack separate a plurality of individual electrolysis cells 2 from one another.
(14) The electrochemical cell 2 is fed with water, which is decomposed at the anode 6b into oxygen gas O.sub.2 and protons H.sup.+. The protons H.sup.+ migrate through the electrolyte membrane 4 in the direction of the cathode 6a. On the cathode side, they recombine to form hydrogen gas H.sub.2.
(15) In another exemplary embodiment, the electrochemical cell 2 is designed as a galvanic cell, or fuel cell, formed for generating electricity. According to the invention, the gas diffusion layers 8 of electrochemical cells 2 formed in this manner are to be modified in a manner analogous to the electrolysis cell shown in
(16) The gas diffusion layer 8 ensures an optimum distribution of the water and also removal of the product gases. In the case of a galvanic cell, the gas diffusion layers 8 accordingly serve for feeding reactants to the respective electrodes. It is essential in this respect that the gas diffusion layer 8 is permeable to the gaseous products or reactants in any case.
(17) The gas diffusion layer 8 moreover serves as a power distributor, particularly in the case of an electrolysis cell. For these reasons, the gas diffusion layer 8 is formed from an electrically conductive, porous material.
(18) In the exemplary embodiment shown, component tolerances, in particular those of the contiguous bipolar plates 10, are compensated for by the gas diffusion layer 8. Therefore, the gas diffusion layer 8 contains layers layered one on top of another, with an outer layer being in the form of a spring component 12a, 12b, 12c (see
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(20) In a first region I, the spring component undergoes a relatively high degree of deformation at a relatively low contact pressure of up to 5 bar; in particular, a deformation of the spring characteristic curve K1 lies between 20% and 30% and a deformation of the spring characteristic curve K2 even lies at up to above 60%.
(21) In a second region II, at a contact pressure of between 5 bar and 25 bar, the deformation of the spring component lies between approximately 60% and approximately 90% with respect to the maximum elastic deformation V.sub.max.
(22) The spring component is moreover configured in such a manner that only a small degree of deformation takes place at a contact pressure of above 25 bar, such that the part of the standardized spring travel S is covered between 60% and 100% for K1 and between approximately 85% and 100% for K2.
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(27) The embodiment of the spring component 12c which is shown in
(28) All of the above-described spring components 12a, 12b, 12c or gas diffusion layers 8 have the property that they compensate for component tolerances which arise in the electrolyzer, in order to allow for uniform contacting of the membrane-electrode-assembly in every instance of tolerance. On account of the progressive spring characteristic curve of the spring components 12a, 12b, 12c, excessive deformation of the gas diffusion layer 8 on one side is prevented in the case of overloading. In all of the embodiments, it is moreover conceivable to arrange a porous diffusion component (not shown in more detail here) between the spring component 12a, 12b, 12c and the contacting component 19, 24, 28.