The invention relates to a gas diffusion layer for an electrochemical cell, in particular for a PEM electrolysis cell. The invention furthermore relates to an electrochemical cell, in particular a PEM electrolysis cell or galvanic cell having such a gas diffusion layer, and also to an electrolyzer.
Electrochemical cells are generally known and are split into galvanic cells and electrolysis cells. An electrolysis cell is an apparatus in which an electric current causes a chemical reaction, with at least some electrical energy being converted into chemical energy. A galvanic cell is an apparatus complementary to the electrolysis cell for spontaneously converting chemical energy into electrical energy. A known apparatus of such a galvanic cell is a fuel cell, for example.
The cleavage of water by electric current for the production of hydrogen gas and oxygen gas by means of an electrolysis cell is well-known. A distinction is made here primarily between two technical systems, alkaline electrolysis and PEM (Proton-Exchange-Membrane) electrolysis.
The core of a technical electrolysis plant is the electrolysis cell, comprising two electrodes and an electrolyte. In a PEM electrolysis cell, the electrolyte consists of a proton-conducting membrane, on both sides of which are located the electrodes. The assembly consisting of membrane and electrodes is referred to as MEA (Membrane-Electrode-Assembly). In the assembled state of an electrolysis stack composed of a plurality of electrolysis cells, the electrodes are contacted by what are termed bipolar plates via a gas diffusion layer, the bipolar plates separating the individual electrolysis cells of the stack from one another. In this case, the O2 side of the electrolysis cell corresponds to the positive terminal and the H2 side corresponds to the negative terminal, separated by the intermediate membrane-electrode-assembly.
The PEM electrolysis cell is fed on the O2 side with fully desalinated water, which is decomposed at the anode into oxygen gas and protons (H+). The protons migrate through the electrolyte membrane and recombine at the cathode (H2 side) to form hydrogen gas. In addition to the electrode contacting, the gas diffusion layer resting on the electrodes ensures an optimum water distribution (and therefore the wetting of the membrane) and also the removal of the product gases. What is therefore required as a gas diffusion layer is an electrically conductive, porous element with good permanent contacting of the electrode. As an additional requirement, dimensional tolerances which possibly arise in the electrolyzer should be compensated for in order to allow for uniform contacting of the MEA in every instance of tolerance.
To date, sintered metal disks have generally been used as the gas diffusion layer. Although these satisfy the requirements in respect of electrical conductivity and porosity, an additional tolerance compensation of the components of the electrolysis cell on both sides of the gas diffusion layer is not possible. Moreover, the manufacturing costs for such disks are comparatively high and there is a restriction with respect to the size owing to the pressing forces required during the manufacture of such disks. In addition, problems in relation to warping which can only be controlled with difficulty arise in the case of large components.
The use of gas diffusion electrodes with resilient elements for producing an electrical contact in the case of alkaline electrolyzers is described, for example, in WO 2007/080193 A2 and EP 2436804 A1.
EP 1378589 B1 discloses a spring sheet, in which the individual spring elements are bent alternately upward and downward. The spring sheet is incorporated in an ion exchange electrolyzer merely on the cathode side, such that the spring sheet contacts the cathodes directly.
US 2003/188966 A1 describes a further spring component for an electrolysis cell, which is arranged between a partition wall and a cathode. The spring component comprises a multiplicity of leaf spring elements, which rest on the cathode for uniform adaptation.
Further gas diffusion electrodes of differing construction are described in WO 2002035620 A2, DE 10027339 A1 and DE 102004023161 A1.
The invention is based on the object of compensating for possible component tolerances in an electrochemical cell, in particular in an electrolysis cell or galvanic cell, in particular in the region of the bipolar plates.
According to the invention, the object is achieved by a gas diffusion layer to be arranged between a bipolar plate and an electrode of an electrochemical cell, comprising at least two layers layered one on top of another, wherein one of the layers is in the form of a spring component having a progressive spring characteristic curve.
According to the invention, the object is furthermore achieved by an electrochemical cell, in particular by a PEM electrolysis cell, having such a gas diffusion layer.
According to the invention, the object is furthermore achieved by an electrolyzer having such a PEM electrolysis cell.
The advantages and preferred embodiments mentioned hereinbelow in relation to the gas diffusion layer can be transferred analogously to the electrochemical cell, the galvanic cell, in particular fuel cell, the PEM electrolysis cell and/or the electrolyzer.
The invention is based on the knowledge that a progressive spring behavior ensures that the contact pressure is sufficient in all tolerance positions of the contiguous components. The implementation of a progressive spring behavior in a gas diffusion layer is effected in this respect by the geometry of the spring component.
A spring component is understood to mean a layer of the gas diffusion layer which has an elastically restoring behavior, i.e. yields under loading and returns to the original shape after relief.
A spring characteristic curve shows the force-travel curve of a spring, i.e. the spring characteristic curve makes a statement in the form of a graph in relation to how efficient the force-travel relationship of a spring is. A progressive spring characteristic curve has the property of showing ever smaller steps on the spring travel with uniform loading steps. In the case of the progressive characteristic curve, the effort exerted increases in relation to the travel covered. As alternatives thereto, there are the linear spring characteristic curve and the degressive spring characteristic curve.
In a possible exemplary embodiment, the gas diffusion layer of the electrochemical cell comprises at least three layers, therefore inner and outer layers. It has proved to be particularly advantageous if the spring component forms an outer layer of the gas diffusion layer.
An “outer layer” is provided to rest against a component adjoining the gas diffusion layer.
In this context an “outer layer” is understood to mean that, in the case of more than two layers, an outer layer which in particular directly adjoins the bipolar plate is in the form of a spring component having a progressive spring characteristic curve.
The use of a spring component having a progressive spring characteristic curve as a gas diffusion layer has the significant advantages that large deformations of the spring component are achieved in the range of the normal contact pressure (approximately 5-25 bar), and therefore high component tolerances are compensated for; in the case of overloading, the additional spring travel is in turn small, and therefore the spring component withstands high pressures. In the case of a load significantly above the operating contact pressure, excessive plastic deformation of the spring component is therefore prevented.
The spring system serves firstly for producing the electrical contacting between the MEA and the bipolar plate, which is already ensured in the case of a small contact pressure. Secondly, the contact pressure ensures uniform and areal contacting with the MEA. Depending on the structural specification, the inflowing water is pre-distributed by the spring component. Furthermore, the flow of electric current is determined via the spring component.
It is preferable that the at least two layers layered one on top of another differ from one another in terms of their structure and/or composition. This is brought about in particular by the functionality of the layers. In the case of a two-layer structure of the gas diffusion layer, one layer lies on the bipolar plate and the other lies on an electrode. The properties and therefore the construction or composition of both layers are correspondingly different. The same applies if one or more intermediate layers are present between the two outer layers.
The gas diffusion layer advantageously comprises three layers: a contacting component, a diffusion component and the spring component. The inner contacting component serves for uniform contacting of the gas diffusion layer on the electrode. The use of fine materials such as, e.g., non-woven material or very finely perforated metal sheet is therefore recommended. The central diffusion component serves to remove gas which forms, with the entire flow of electric current also passing said component. As already explained, the outer spring component ensures first and foremost the most stable contact pressure possible, irrespective of the tolerance position of the adjoining components.
With a view to a particularly high degree of flexibility of the spring component, which satisfies the requirements during use with respect to the tolerance compensation, the spring component is configured in such a manner that the spring characteristic curve can be divided into at least two, in particular three, regions of differing progression. In this case, the spring component is characterized by a maximum elastic deformation in the region of the greatest contact pressure. In this case, maximum elastic deformation is understood to mean the boundary between an elastic and purely plastic behavior of the spring component. A part-elastic and part-plastic behavior of the spring component likewise falls under the maximum elastic deformation here. In particular, the maximum elastic deformation travel of the spring component is achieved at a contact pressure of approximately 50 bar. At above approximately 50 bar, the spring has a purely plastic behavior, i.e. the deformation at this loading and above is irreversible.
With a view to a rapid compensation of component tolerances, the spring component is preferably configured in such a manner that, with a contact pressure of up to 5 bar, there is deformation of the spring component amounting to up to 60%, in particular up to 80%, with respect to the maximum elastic deformation.
Moreover, the spring component is preferably configured in such a manner that, with a contact pressure of between 5 bar and 25 bar, there is deformation of the spring component (12a, 12b, 12c) amounting to between 60% and 90% with respect to a maximum elastic deformation.
The spring component is expediently formed from an electrically conductive material, in particular from high-grade steel, titanium, niobium, tantalum and/or nickel. Such a composition of the spring component allows it to be used in particular as a power distributor.
According to a first preferred embodiment, the spring component is formed in the manner of a profiled metal sheet. Such an embodiment is distinguished by a comparatively easy production.
According to an alternative preferred embodiment, the spring component is formed in the manner of a mesh. in this case, the spring properties can easily be varied by the manner and density of the mesh.
The spring component preferably comprises one or more spirals. The spring properties are defined in this case by the design and arrangement of the spirals.
Exemplary embodiments of the invention can be explained with reference to a drawing, in which:
Identical reference signs have the same meaning in the various figures.
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.
The electrochemical cell 2 is fed with water, which is decomposed at the anode 6b into oxygen gas O2 and protons H. The protons H+ migrate through the electrolyte membrane 4 in the direction of the cathode 6a. On the cathode side, they recombine to form hydrogen gas H2.
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
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.
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.
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
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%.
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 Vmax.
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.
The embodiment of the spring component 12c which is shown in
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.
Number | Date | Country | Kind |
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14172465.8 | Jun 2014 | EP | regional |
Filing Document | Filing Date | Country | Kind |
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PCT/EP2015/063262 | 6/15/2015 | WO | 00 |