Patent Application
20230022392
The present invention relates to a sensor device for a fuel cell system, a fuel cell system with such a sensor and a method for controlling a purging process of a fuel cell system.
It is known that fuel cells perform a recirculation of fuel during operation. The fuel is, for example, hydrogen, which is fed to an anode side of the fuel cell and chemically reacted there. However, in the usual mode of operation, a residue of the fuel remains in the anode exhaust gas after the anode. In order to be able to reuse this remaining residual fuel, it is known for at least a part of the anode exhaust gas to be returned to the anode feed section in a recirculation section.
A disadvantage of the known solutions is that contamination can occur in the anode feed section and thus in the anode of the fuel cell stack due to the recirculation described above. Through diffusion processes, it is possible that nitrogen can get into the anode exhaust gas and is fed back into the anode feed section through the recirculation and as a result thus also accumulates. Water or water vapour can also be found in an anode exhaust gas which is also fed in liquid form, as droplets, into the anode feed section through the recirculation, where it can also block paths in the hydrogen path. Furthermore, due to damage mechanisms, small amounts of carbon monoxide and carbon dioxide can form on the anode side. In order to avoid an excessive degree of contamination in the gas of the anode feed section, a purging process is therefore carried out in the known fuel cell systems. A distinction is made in particular between purging and bleeding processes. Purging processes involve a short-term draining or purging of the anode feed section, while a bleeding process is understood to mean a longer-term draining or purging with low volume flows.
In the known solutions, the timing of the purging process is either initiated if the cell voltage of individual cells of the fuel cell stack falls below a certain level or is determined algorithmically on the basis of a simulation model. This simulates which impurities are produced in the anode feed section, over which period of operation and under which operating conditions. The purging process is then carried out on the basis of this simulation result. In order to avoid a summing-up of simulation errors, a larger number of purging processes is carried out, to be on the safe side. On the one hand, this is disadvantageous since it limits the operation of the fuel cell. A further disadvantage is anode feed gas which is lost in this way, i.e. lost fuel that is no longer available for electricity generation.
It is the object of the present invention to remedy, at least partially, the disadvantages described above. In particular, it is the object of the present invention to improve the control of the purging process in a fuel cell system in a cost-effective and simple way.
The above object is achieved by a sensor device with the features of claim 1, a fuel cell system with the features of claim 9 and a method with the features of claim 13.
Further features and details of the invention emerge from the dependent claims, the description and the drawings. Features and details which are described in connection with the sensor device according to the invention naturally also apply in connection with the fuel cell system according to the invention as well as the method according to the invention and vice versa, so that with regard to disclosure, mutual reference is or can always made to the individual aspects of invention.
According to the invention, a sensor device for a fuel cell system is designed to determine a purging parameter for controlling a purging process of the fuel cell system. For this purpose, the sensor device has a first flow channel for arranging in an anode feed section of an anode section of a fuel cell stack. The sensor device is also equipped with a second flow channel for arranging in a recirculation section of the anode section of the fuel cell stack. The first flow channel and the second flow channel are separated from each other, at least in sections, by means of a gas-tight membrane. This membrane is designed to be permeable for protons and has an electrode section on both sides. The sensor device also has a measuring device for determining a fuel concentration difference, in particular of hydrogen, between the first flow channel and the second flow channel, as a purging parameter, based on an electrical voltage between the two electrode sections.
Within the context of this application, the functionality is explained in part on the basis of hydrogen as fuel. Naturally, the use of other fuels is also possible within the scope of the present invention.
In contrast to the known solutions, a sensor device is now designed to perform an integral determination of the fuel concentration difference between the two flow channels and thus between the anode feed section and the recirculation section. This is based in particular on the idea that the concentration in the anode feed section is basically known, since this is the supply of the fuel. If, for example, hydrogen is used as fuel, it can be assumed that a one hundred percent or virtually one hundred percent hydrogen concentration is present in the anode feed section. The hydrogen concentration in the recirculation section depends on how large the degree of contamination is. Over the course of operation of the fuel cell, the impurities add up, so that the proportion of the contamination increases, as a result of which the proportion of hydrogen in the recirculation section decreases.
By means of a sensor device according to the invention, it is now possible to determine this concentration difference. This is based on an electrical potential between the first flow channel and the second flow channel. If there is a hydrogen concentration difference between the first flow channel and the second flow channel, this has effects on the membrane and the electrode sections placed thereon. The concentration difference leads to the protons and electrons in the first flow channel formed from the hydrogen, in particular on a catalyst layer, being moved through the membrane, which is designed to be permeable for protons, and electrodes which are conductive for the electrons in order to produce a chemical concentration balance with respect to the second flow channel. Because these protons have to move in order to pass through the membrane, and also because the electrons have to move through the two electrode sections, an electrical potential is created between the electrode section in the first flow channel and the electrode section in the second flow channel. This electrical potential described above can be measured between the two electrode sections via the measuring device and, as an electrical voltage, define a purging parameter. The measured electrical voltage between the two electrodes can be used directly as purging parameter. However, a further processing of this determined voltage value can also take place in order to allow a conclusion to be drawn as to the concentration difference and in particular a determination of the actual concentration of hydrogen in the second flow channel.
Based on the above explanation, the sensor device can thus be integrated into the fuel cell system. It is thus possible to monitor the concentration differences between the first flow channel and the second flow channel integrally within the fuel cell system and in particular in a continuous or substantially continuous manner. In addition to simply monitoring the difference, on the basis of a known concentration in the anode feed section a quantitative determination or at least a quantitative approximation of the hydrogen concentration in the recirculation section can actually take place. In contrast to the known solutions, it is no longer necessary to resort to a simulation model to start the purging processes. Rather, a determination of the hydrogen concentration and thus also a conclusion as to the degree of contamination in the recirculation section is possible. The degree of contamination can now be used as a control parameter to trigger a purging process.
The integral determination of a purging parameter on the basis of actually existing and measured differences in the concentration of hydrogen means that unnecessary purging processes can be avoided. Instead, it is sufficient if purging is carried out precisely when the degree of contamination of the recirculation gas exceeds a predefined degree, for example a specified value. Such targeted purging processes thus avoid unnecessary purging processes carried out for precautionary reasons on the basis of simulation results, so that the hydrogen loss due to such unnecessary purging processes can also be avoided. In addition, due to the precise knowledge of the concentration, in particular in the recirculation section, a significantly more dynamic control of the hydrogen supply in the anode feed section, in particular from a hydrogen source, is possible. This means that a load requirement for the fuel cell can be varied more dynamically and, above all, more flexibly. Last but not least, it should also be pointed out that targeted purging processes reliably avoid an excessive degree of contamination, in particular an excessive degree of nitrogen in the recirculation section and thus also in the anode feed section. An excessive nitrogen content could otherwise lead to degradation of the anode section of the fuel cell stack.
For the arrangement of the sensor device within the anode feed section and within the recirculation section, the respective flow channels are preferably designed with corresponding inputs and outputs in order to be integrated in a fluid-communicating manner in the anode feed section and the recirculation section. The first flow channel is designed to be gas-tight with respect to the second flow channel.
It can bring advantages if, in a sensor device according to the invention, the electrode sections cover the entire membrane or substantially the entire membrane on both sides. This is to be understood to the effect that no bypass of protons next to the electrodes is possible. In addition, a simple means of producing the membrane can be made available in this way, since this can also be produced in large sheets and then cut to size. By avoiding the bypass for protons described above, a significantly more accurate measurement and thus an improved determination of the purging parameter is possible.
Further advantages can be achieved if, in a sensor device according to the invention, the first flow channel and the second flow channel are identical or substantially identical in design, in particular with respect to the flow conditions. This includes, for example, identical flow cross-sections of the two flow channels. Identical or substantially identical design can also be understood to include identical overall volumes of the two flow channels. In particular, wall surfaces that influence the flow in the two flow channels as well as the corresponding inlet and outlet cross-sections are also identical or substantially identical. This means that a simplified evaluation of the determined concentration differences or the electrical voltage determined by means of the measuring device is possible.
In addition, it is also advantageous if, in a sensor device according to the invention, the first flow channel and/or the second flow channel have at least one actuating device for controlling the flow conditions in the respective flow channel. Such an actuating device can, for example, be designed as a valve or as a pump and leads to an equalisation of the flow conditions on both sides. In order to make possible an improved and above all a simplified evaluation for the purging parameter on the measuring device, the flow conditions in the two flow channels can be actively adapted. In particular, if the degree of recirculation is changed an equalisation of the flow conditions in the sensor device can be made available with the help of the actuating device. Even if different flow conditions arise due to different feed speeds or feed mass flows in the anode feed section under different load conditions or load requirements for the fuel cell system, an equalisation of the flow conditions can be made possible through the corresponding actuating device in the second flow channel.
It is also advantageous if, in a sensor device according to the invention, the at least one actuating device comprises at least one of the following modules:
The above list is a non-exhaustive list. A pressure module or a mass flow module can for example be understood to mean pump devices, pressure control devices or control valves. This makes it possible to influence the gas pressure and/or the mass flow, preferably both, in the respective flow channel and to adapt these to the corresponding conditions in the other flow channel. Preferably, such actuating devices are provided for both flow channels to provide a greater flexibility in the variation of the flow conditions and in the possibility of equalisation.
It is also advantageous if, in a sensor device according to the invention, the membrane has on at least one side, in particular on both sides, preferably on the respective electrode section, a catalyst layer for oxidising gas components, in particular hydrogen. This oxidation is to be understood as a chemical oxidation, so that, for example, protons and electrons are generated from hydrogen. The catalytic conversion of gas components through chemical oxidation means that even further improved preconditions for the formation of an electrical voltage are provided through a chemical potential between the two flow channels. In particular, the catalyst layers on both electrode sections are identical or substantially identical in form.
It can also be advantageous if, in a sensor device according to the invention, the membrane is designed to be electrically insulating. This can be made available through appropriate material properties of the membrane. However, it is also conceivable that the membrane provides the electrical insulation via a coating or a corresponding connection to walls or to a housing. It is particularly preferred if the membrane is in correspondingly electrically-insulating contact with one or even two electrode sections.
It is also advantageous if, in a sensor device according to the invention, the first flow channel and the second flow channel flow along the membrane in parallel. This means that concentration shifts which are otherwise possible due to counterflow are avoided and an undesirable variation due to temperature differences within the two flow channels is reduced.
The object of the present invention also includes a fuel cell system having
A sensor device according to the present invention is thereby provided. The anode feed section contains the first flow channel of the sensor device and the recirculation section contains the second flow channel of the sensor device. Thus, a fuel cell system according to the invention brings the same advantages as have been explained in detail in relation to a sensor device according to the invention. Naturally, the fuel cell system can have even more features. For example, the sensor section may be arranged upstream of a reformer device which converts supplied reformer feed gas into a reformed anode feed gas. Further components such as heat exchangers, afterburners or pole burner devices can also be used in such a fuel cell system within the scope of the present invention.
It can also be advantageous if, in a fuel cell system according to the invention, a mixing section is arranged downstream of the flow direction of the recirculated anode exhaust gas to introduce the recirculated anode exhaust gas into the anode feed section. In other words, a mixing of the recirculation gas and the anode feed gas takes place in the mixing section. This makes possible a simple and cost-effective mixing and combination of these two gases. The arrangement downstream of the second flow channel means that the mixing takes place after the determination of the purging parameter according to the invention has taken place. In addition to a mixing, a separate line leading to the anode section from the second flow channel would also be conceivable within the scope of the present invention.
It also brings advantages if, in a fuel cell system according to the invention, the mixing section in the anode feed section is arranged downstream of the first flow channel in the flow direction of the anode feed gas. This means that only after the anode feed gas has flowed through the first flow channel does a mixture with the recirculation gas take place. The influence of the recirculation gas and thus the resulting mixing concentration thus only takes place when the first flow channel has already been passed. This means that an exact composition can in particular be determined for the recirculation gas if the pure anode feed gas is known and this also flows in pure form through the first flow channel. In this way, undesirable cross-influences and deviations that build up over time are avoided for the first flow channel.
It can also be advantageous if, in a fuel cell system according to the invention, the mixing section in the anode feed section is arranged upstream of the first flow channel in the flow direction of the anode feed gas. This makes it possible to compare, not the pure gas component of the anode feed gas, but rather the already-adjusted mixture with the recirculation gas. This is particularly advantageous if not only one sensor device but two sensor devices are provided. For example, it brings great advantages if a first sensor device is arranged before the mixing section and a second sensor device after the mixing section, so that it becomes possible to provide both a comparison with the pure anode feed gas and with the mixed anode feed gas via chemical potential detection and corresponding purging parameters.
The object of the present invention also includes a method for controlling a fuel cell system according to the invention, having the following steps:
A method according to the invention thus brings the same advantages as have been explained in detail in relation to a fuel cell system according to the invention. A purging process can thereby be a purging process or also a bleeding process. It is also conceivable that the purging parameter or the degree of deviation from the specified value decides whether a purging process or a bleeding process should be carried out.
It is also advantageous if, in a method according to the invention, a secondary parameter, in particular in the form of a nitrogen concentration in the second flow channel, is determined on the basis of the purging parameter. This is particularly advantageous if pure or substantially pure anode feed gas, for example pure hydrogen, is present in the first flow channel. The secondary parameter can thus generate, as a difference, the exact percentage of contamination, in particular in the form of nitrogen, without the nitrogen or nitrogen content having to be determined directly. The secondary parameter can be used on its own, but also combined with the purging parameter, as the comparison value in order to control the purging process.
Further advantages, features and details of the invention emerge from the following description, in which exemplary embodiments of the invention are described in detail with reference to the drawings. The features mentioned in the claims and in the description can in each case be essential to the invention, taken individually or in any combination. In each case schematically:
The above explanation describes the present invention exclusively in the context of examples. Naturally, individual features of the present embodiments can be combined with each other freely without departing from the scope of the present invention.
| Number | Date | Country | Kind |
|---|---|---|---|
| A51114/2019 | Dec 2019 | AT | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/AT2020/060482 | 12/18/2020 | WO |
