• 专利附录
  • 专利说明
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  • 类似技术
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    • 专利摘要:
    The present invention relates to a fuel cell system (100) comprising at least one fuel cell stack (1) having a first electrode (2) and a second electrode (3), an air supply section (10) for supplying air (30) to the first electrode (2) a Nutzgaszuführabschnitt (11) for supplying Nutzgas (31) to the second electrode (3), an exhaust air section (12) for discharging exhaust air (32) from the first electrode (2), a Nutzabgasabschnitt (13) for discharging Nutzabgas ( 33) of the second electrode (3), wherein the exhaust air section (12) and the Nutzabgasabschnitt (13) in an exhaust gas burner (4) for at least partially catalytic combustion of the exhaust air (32) and the Nutzabgases (33) open, and a burner exhaust gas section ( 17) having a first burner exhaust branch (18) and a second burner exhaust branch (19) for discharging burner exhaust gas (34) from the exhaust gas burner (4), wherein the first burner exhaust branch (18) with a first heat exchanger element (5) in L air supply section (10) for providing heat energy to the air (30) in the air supply section (10) and the second burner exhaust branch (19) with a second heat exchanger element (6) in the Nutzgaszuführabschnitt (11) for providing heat energy to the Nutzgas (31) in the Nutzgaszuführabschnitt (11) is connected. Furthermore, the present invention relates to a method for operating a fuel cell system (100).
    公开号:AT521207A1
    申请号:T503722018
    申请日:2018-05-03
    公开日:2019-11-15
    发明作者:Ing David Reichholf Dipl；Ing Dipl (Fh) Richard Schauperl；Franz Koberg Bsc；Zehetner Alexander；Bernd Reiter Bsc；Ing Dr Martin Hauth Dipl
    申请人:Avl List Gmbh；
    IPC主号:
    专利说明:

    Summary
    The invention relates to a fuel cell system (100), comprising at least one fuel cell stack (1) with a first electrode (2) and a second electrode (3), an air supply section (10) for supplying air (30) to the first electrode (2) , a useful gas supply section (11) for supplying useful gas (31) to the second electrode (3), an exhaust air section (12) for removing exhaust air (32) from the first electrode (2), a useful exhaust gas section (13) for removing useful exhaust gas ( 33) from the second electrode (3), the exhaust air section (12) and the useful exhaust gas section (13) opening into an exhaust gas burner (4) for at least partially catalytic combustion of the exhaust air (32) and the useful exhaust gas (33), and a burner exhaust gas section ( 17) with a first burner exhaust branch (18) and a second burner exhaust branch (19) for removing burner exhaust gas (34) from the exhaust burner (4), the first burner exhaust branch (18) having a first heat exchanger element (5) in the left air supply section (10) for providing thermal energy to the air (30) in the air supply section (10) and the second burner exhaust branch (19) with a second heat exchanger element (6) in the useful gas supply section (11) for providing thermal energy to the useful gas (31) in the useful gas supply section (11) is connected. The invention also relates to a method for operating a fuel cell system (100).
    Fig. 1/37
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    Fuel cell system and method for operating a fuel cell system
    The present invention relates to a fuel cell system, comprising at least one fuel cell stack with a first electrode and a second electrode, an air supply section for supplying air to the first electrode, a useful gas supply section for supplying useful gas to the second electrode, an exhaust air section for removing exhaust air from the first electrode , a useful exhaust gas section for removing useful exhaust gas from the second electrode, the exhaust air section and the useful exhaust gas section opening into an exhaust gas burner for at least partially catalytic combustion of the exhaust air and the useful exhaust gas, and a burner exhaust gas section with a first burner exhaust gas branch and a second burner exhaust gas branch for removing burner exhaust gas from the exhaust gas burner , wherein the first burner exhaust branch with a first heat exchanger element in the air supply section for providing thermal energy to the air in the air supply section and the second burner exhaust branch with e is connected in a second heat exchanger element in the useful gas supply section to provide thermal energy to the useful gas in the useful gas supply section. The present invention further relates to a method for operating such a fuel cell system.
    In modern technology, it is known to use fuel cell systems, often comprising one or more fuel cell stacks, each with a large number of fuel cells, in mobile and stationary applications. Such fuel cell systems usually also have a plurality of subsystems or subunits. In particular, the already mentioned at least one fuel cell stack with one or more fuel cells, supply devices for the fluids required in the fuel cell stack, discharge devices for removing the reaction products generated in the fuel cell stack, which are usually also present as fluids, can be present as subunits. Further possible subsystems can include, for example, an exhaust gas burner for at least partially catalytic combustion of reaction products generated in the fuel cell stack, a start burner for supporting a starting process of the fuel cell system or also a reformer for providing or converting useful gas required in the fuel cell stack.
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    The entire fuel cell system and in particular its subsystems have different requirements with regard to a temperature or a thermal level that the individual subunits of the fuel cell system require for the most efficient operation of the fuel cell system. In particular when using solid fuel cells (SOFC), which often have an operating temperature of 600 ° C to 1000 ° C, it is necessary to maintain the required temperature level (s) for an efficient operation of a fuel cell system. Furthermore, the temperature level to be provided in the fuel cell system can also be influenced by the operating mode in which the fuel cell system is to be operated. For example, a fuel cell system for generating electrical energy can be operated using air and useful gas, but to the contrary in an operating mode in which the fuel cell system produces useful gas, such as hydrogen and / or carbon monoxide, using electrical energy.
    According to the prior art, it is known in particular to use electrical heating devices in order to provide and control the temperature required in each case in the interior of a fuel cell system. It has been found to be disadvantageous here that these electrical heaters, in particular, consume electrical energy, as a result of which an overall efficiency when operating a fuel cell system is reduced. In addition, electric heaters and their use are not ideal because energy has to be transferred to an operating fluid. The transmission path leads to relevant heat losses, which negatively affect system efficiency. In addition, the electrical heating devices in turn mostly represent independent subsystems for a fuel cell system, so that the number of components required to operate a fuel cell system is increased. This can also lead to disadvantages, for example in terms of time and cost in the manufacture of a fuel cell system. A susceptibility to wear and / or a need for regular maintenance of the fuel cell system, in particular a shortening of maintenance intervals, can also be due to the use of electrical heating devices.
    The object of the present invention is to at least partially take into account the problems described above or at least alternative / 37
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    To create solutions. In particular, it is an object of the present invention to provide a fuel cell system and a method for operating a fuel cell system which, in a particularly simple and cost-effective manner, improve a fuel cell system and a method for operating a fuel cell system in such a way that setting required temperatures or temperature levels is achieved in the fuel cell system, in particular for the individual subunits of the fuel cell system, can be simplified in order to simplify operation of the fuel cell system as a whole and to increase overall efficiency when operating the fuel cell system.
    The above object is solved by the claims. In particular, the above object is achieved by the fuel cell system according to independent claim 1 and by the method according to independent claim 15. Further advantages of the invention result from the subclaims, the description and the drawings. Features and details that are described in connection with the fuel cell system according to the invention apply, of course, also in connection with the method according to the invention for operating a fuel cell system and vice versa, so that with respect to the disclosure of the individual aspects of the invention, reference is always or can be made to one another.
    According to a first aspect of the invention, the object is achieved by a fuel cell system comprising at least one fuel cell stack with a first electrode and a second electrode, an air supply section for supplying air to the first electrode, a useful gas supply section for supplying useful gas to the second electrode, and an exhaust air section for Removing exhaust air from the first electrode, a useful exhaust gas section for removing useful exhaust gas from the second electrode, the exhaust air section and the useful exhaust gas section opening into an exhaust gas burner for at least partially catalytic combustion of the exhaust air and the useful exhaust gas, and a burner exhaust gas section with a first burner exhaust gas branch and a second Burner exhaust branch for removing burner exhaust from the exhaust burner, the first burner exhaust branch having a first heat exchanger element in the air supply section for providing thermal energy to the air in the air supply section and the second burner exhaust branch / 37
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    AVL List GmbH is connected to a second heat exchanger element in the useful gas supply section for providing thermal energy to the useful gas in the useful gas supply section. A fuel cell system according to the invention is characterized in that the fuel cell system has a distribution system with flow control means at least in the useful exhaust gas section and in the burner exhaust gas section for distributing thermal energy stored in the useful exhaust gas and / or in the burner exhaust gas in the fuel cell system.
    A fuel cell system according to the invention in particular has at least one fuel cell stack with a first electrode and a second electrode as the core piece. The electrodes are preferably separated from one another by an electrolyte. The at least one fuel cell stack itself can in turn consist of one or more fuel cells, which in turn each have a first electrode and a second electrode. Solid fuel cells (SOFC) can preferably also be used as fuel cells in a fuel cell stack of a fuel cell system according to the invention. The first electrode is connected in a fluid-communicating manner on an input side to an air supply section and on an output side to an exhaust air section. In other words, air, in particular ambient air, which preferably has oxygen, can be supplied to the first electrode via the air supply section. This oxygen in particular can react in the first electrode and, for example, emit electrons and diffuse as charged ions through the electrolyte to the second electrode. Reaction products and unused air can be conducted away from the first electrode as exhaust air through the exhaust air section. Similarly, the second electrode also has an input side and an output side. The input side of the second electrode is connected to a useful gas supply section, the output side to a useful exhaust gas section. Commercial gas, for example carbon monoxide, hydrogen, methane or the like, can be fed to the second electrode in this way. Accordingly, the useful gas can then react in the second electrode, for example with the oxygen ions diffused through the electrolyte, it being possible for corresponding reaction products and unused useful gas to be removed again from the second electrode through the useful exhaust gas section. In particular, a fuel cell system according to the invention can preferably be used both for generating electrical energy and for producing useful gas while consuming electrical energy. With a generation / 37
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    AVL List GmbH electrical energy forms in particular the first electrode a cathode side and the second electrode an anode side of the fuel cell stack. Conversely, when useful gas is produced using electrical energy, the first electrode forms the anode and the second electrode forms the cathode of the fuel cell stack.
    Another element of a fuel cell system according to the invention is an exhaust gas burner into which the exhaust air section and the useful exhaust gas section open. In this way, the exhaust air and the useful exhaust gas can be fed to the exhaust gas burner, whereby an at least partially catalytic combustion of these two fluids is possible. In addition to the often heat-generating reactions in the fuel cell stack itself, this at least partially catalytic combustion of the fuel components by gases and the combustion of the fuel components in the useful exhaust gas with oxygen represent a further source of thermal energy in the fuel cell system, with this thermal utilization of the exhaust air and the useful exhaust gas already an overall efficiency in the operation of a fuel cell system according to the invention can be further increased. An advantage compared to the use of electric heaters is the direct heat generation in the fluid, so that practically no transmission path is necessary, as a result of which heat losses are avoided.
    The heat generation in the fuel cell stack is fundamentally dependent on an operating mode of the same and can take place through reactions and voltage losses in the fuel cell mode or only through voltage losses in the electrolysis mode. In the fuel cell mode, heat is generated by the voltage losses and the exothermic reactions, whereas in the electrolysis mode, heat is generated predominantly or exclusively by voltage losses, since endothermic reactions take place here.
    Downstream from the exhaust gas burner, it is provided in particular that the burner exhaust gas is discharged from a burner exhaust gas section, this burner exhaust gas section being divided into a first burner exhaust gas branch and a second burner exhaust gas branch. Each of these burner exhaust gas branches leads burner exhaust gas to a heat exchanger element, in particular a first heat exchanger element in the air supply section and a second heat exchanger element in / 37
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    Commercial gas supply section. This makes it possible to provide thermal energy for heating both the air and the useful gas, both of which are supplied to the fuel cell stack. A general recycling of the thermal energy generated in the exhaust gas burner can already be provided in this way.
    Essential to the invention, a fuel cell system according to the invention also has a distribution system. This distribution system in particular comprises flow control means at least in the useful exhaust gas section and in the burner exhaust gas section. Such flow control means can be used in particular to adjust or control, in particular, an amount and / or speed of the fluid flowing in the respective section. By arranging the flow control means at least in the useful exhaust gas section and in the burner exhaust gas section, it is thus possible to provide that a quantity of both the useful exhaust gas, which is heated up by the reactions in the fuel cell system and thus has a large amount of stored thermal energy, and of the burner exhaust gas, which is likewise produced by the at least partially catalytic combustion of the exhaust air and the useful exhaust gas is heated and carries a large amount of stored thermal energy in a targeted manner. In other words, the distribution system of a fuel cell system according to the invention can provide a targeted, in particular customized, distribution of the thermal energy already present in the fuel cell system or in the fluids of the fuel cell system.
    For this purpose, a distribution system according to the invention is preferably designed to identify a heat energy requirement in the fuel cell system. Such a demand for thermal energy in the fuel cell system can be characterized in particular by a location in the fuel cell system and a size of the demand. A distribution system according to the invention can also be used to determine where and how much thermal energy is present in the fuel cell system, in particular in the fluids of the fuel cell system. Appropriate control of the flow control means of the distribution system can then be used to carry out a distribution of the heat energy stored in the fluids of the fuel cell system, as required. In addition to the pure supply of hot fluids to heat exchangers, a distribution system according to the invention can therefore be used to match supply and thus an even better supply
    PP31957AT
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    Distribution of thermal energy can be provided inside a fuel cell system. An increase in the overall efficiency when operating a fuel cell system according to the invention can be achieved in this way. In particular, it can also be avoided that the necessary thermal energy has to be provided alone or at least mainly by external devices, such as electrical heating devices. A structure of a fuel cell system according to the invention can thereby be simplified.
    In a fuel cell system according to the invention, it can particularly preferably be provided that the distribution system has sensor means and an evaluation unit for determining a temperature requirement of the fuel cell system. In this way, in particular an integration of such sensor means, for example temperature sensors, and an evaluation unit, for example a computer unit, can be provided in the entire distribution system. The sensor means can preferably be arranged in particular at those points of the fuel cell system where either a temperature requirement is expected, for example on and / or in a reformer, an evaporator and / or heat exchanger, or at which thermal energy is generated and / or provided, for example the exhaust air section, the useful exhaust gas section and / or the exhaust gas burner. Comprehensive recording of a temperature requirement by evaluating the sensor data of the sensor means in the evaluation unit can be made possible in this way. In addition, the integration can also provide a particularly compact structure of a distribution system according to the invention and thereby of a fuel cell system according to the invention. Furthermore, a distribution system according to the invention can also include corresponding communication means between the sensor means, the flow control means and the evaluation unit. Communication means in the sense of the invention can in particular represent wired and / or wireless communication paths.
    A fuel cell system according to the invention can also be characterized in that the flow control means comprise at least one controllable first valve in the useful exhaust gas section, a controllable second valve in the first burner exhaust gas branch and a controllable third valve in the second burner exhaust gas branch. The useful exhaust gas section and in particular the burner exhaust gas branches carry fluids or gases of the fuel cell system, / 37 with the useful exhaust gas and the burner exhaust gas
    PP31957AT
    AVL List GmbH which have a particularly high temperature and therefore carry a particularly high thermal energy. A need-adjusted distribution of this thermal energy in the fluids in the above-mentioned line sections of a fuel cell system according to the invention can be provided particularly easily by valves in these line sections. Thus, the exhaust gas section feeds the exhaust gas burner to the exhaust gas section. A quantity of this useful exhaust gas can thus be controlled or regulated by the first valve. An increase in the amount of useful exhaust gas usually leads to an increase in the exhaust gas burner temperature and thereby in the burner exhaust gas. On the contrary, a reduction in an amount of useful exhaust gas when the first valve is at least partially closed can lead to a reduction in the exhaust gas burner temperature and thereby in the temperature of the burner exhaust gas. The second and the third valve are each arranged in a burner exhaust branch, each of these burner exhaust branches comprising at least one heat exchanger element, the first exhaust branch with regard to the air supply section, the second burner exhaust branch with regard to the useful gas supply section. A quantity of burner exhaust gas that is fed to the heat exchanger in the air supply can thus be controlled and / or regulated by a second valve. Analogously, the third valve can be used to control and / or regulate an amount of burner exhaust gas which is fed to the heat exchanger in the useful gas feed line, wherein this heat exchanger can also be designed as a reformer. Overall, the three valves described can thus be used to provide a differentiated distribution and control or regulation of the existing or generated thermal energy in the fuel cell system according to the invention in a particularly simple manner.
    According to a further development of a fuel cell system according to the invention, it can further be provided that the second valve is arranged in the first burner exhaust branch downstream of the first heat exchanger element and / or that the third valve is arranged in the second burner exhaust branch downstream of the second heat exchanger element. In these particularly preferred arrangements, the valves are each arranged downstream of a heat exchanger element, as a result of which an at least partial release of thermal energy from the fluid flowing in the respective burner exhaust gas branch has already taken place in the heat exchanger element. In other words, the fluid flowing in the respective burner exhaust gas branch has at least partially already cooled, so that / 37
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    AVL List GmbH a requirement on the second valve and / or third valve with regard to temperature resistance can be reduced. The use of simpler and therefore usually cheaper valves can be provided in this way.
    A fuel cell system according to the invention can also be designed such that the fuel cell system has a burner air supply that branches off, in particular, from the air supply section, the burner air supply opening into the exhaust gas burner. In this way it is possible, in particular, to supply the exhaust gas burner with fresh air in addition to the exhaust air from the fuel cell stack. This additional supply of air, which usually has a lower temperature than the exhaust air and / or the useful exhaust gas, allows a combustion temperature of the exhaust gas burner to be changed, in particular reduced. In particular, excessively high temperatures in the exhaust gas burner, which in the worst case can lead to damage to the exhaust gas burner, can be avoided in this way. An even more efficient operation of the exhaust gas burner can be provided in this way, as a result of which an overall efficiency of the fuel cell system according to the invention can also be increased.
    According to a preferred further development of a fuel cell system according to the invention, it can further be provided that the flow control means comprise a fourth valve for adjusting an amount of the air conveyed in the burner air supply and / or a heating element in the burner air supply for heating the air conveyed in the burner air supply. A fourth valve of this type can be used, in particular, to set a quantity of the air additionally supplied to the exhaust gas burner. A heating element in turn enables a temperature to be controlled or regulated by the additional air supplied to the exhaust gas burner. Controlling or regulating a setting of an exhaust gas burner temperature and thereby the temperature or the thermal energy content of the burner exhaust gas can be further improved in this way. An even better and needs-based distribution of the thermal energy in the fuel cell system can be made possible in this way.
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    Furthermore, it can be provided in a fuel cell system according to the invention that the flow control means comprise an air supply fan in the air supply section for setting an amount of the air conveyed in the air supply section. Such an air supply fan can thus be used, in particular, to adjust a quantity of air supplied, both to the fuel cell stack and, if present, via a burner air supply to the exhaust gas burner. As already described above, this air supply can be used, at least indirectly, to control a temperature both in the fuel cell stack and, if appropriate, in the exhaust gas burner. It is also possible to control and / or regulate a reaction rate in the fuel cell stack by means of a controlled change in the amount of air supplied by the air supply to the first electrode. A distribution of thermal energy in the fuel cell system according to the invention can thus be provided, at least indirectly, by a flow control means designed as an air supply fan, in particular by controlling and / or regulating a thermal energy generated in the fuel cell system.
    In a fuel cell system according to the invention, it can preferably also be provided that the fuel cell system has an evaporator for providing water vapor for introduction into the useful gas supply section, the evaporator for transmitting thermal energy stored in the useful exhaust gas and / or in the burner exhaust gas downstream of the useful exhaust gas section and / or downstream of the first Burner exhaust branch and / or downstream of the second burner exhaust branch is arranged. Such an evaporator represents a possible consumer of thermal energy present in the fuel cell stack, as a result of which it is advantageous to include such an evaporator in a distribution system according to the invention. In this way, it can in particular be provided that thermal energy already present in the fuel cell system can be used to evaporate fluid, preferably for example water, in the evaporator, which can enable a further increase in overall efficiency when operating a fuel cell system according to the invention. This can in particular be provided in that the evaporator for transferring thermal energy in the respective fluid is arranged downstream on the useful exhaust gas section and / or at least one of the burner exhaust gas branches. As already described above, the useful exhaust gas section and the burner exhaust gas branches represent those line sections in which fluids with the highest temperatures and thus the highest / 37
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    AVL List GmbH stored heat energy, especially useful exhaust gas or burner exhaust gas. A particularly good and efficient evaporation of, for example, water to water vapor in the evaporator, particularly preferably without additional, externally provided energy, can be provided in this way.
    A fuel cell system according to the invention can particularly preferably be developed in such a way that the evaporator is designed as a two-stage evaporator. In the sense of the invention, two-stage means in particular that there are two stages in the evaporator, each with a heat exchanger through which a heating medium flows, with a first stage preferably already being designed for partial evaporation of the fluid and complete evaporation being achievable or achieved with a second stage . A transition from the first stage to the second stage advantageously takes place in two phases or as a two-phase mixture. The second stage is arranged downstream of the first stage with respect to a flow direction of the fluid to be evaporated in the evaporator. The fluid to be evaporated is thus evaporated in both stages, wherein this is preferably only partially evaporated in the first stage and is also overheated in the second stage. In principle, however, it can also be provided that the first stage is used only for heating the fluid of the evaporator to be evaporated, and the second stage, which is arranged downstream of the first stage with respect to a direction of flow of the fluid to be evaporated in the evaporator, is used for actual evaporation.
    A two-stage embodiment of an evaporator is particularly advantageous in operating situations of a fuel cell system if neither of the two heating media used in the two stages of the evaporator alone would be sufficient, for example with regard to a thermal energy stored in the heating media, in order to evaporate the fluid to be evaporated, in particular water. and in particular, for example, it is also not possible to merge the preferably different heating media. Furthermore, such a two-stage evaporator can also be used for control purposes. Control option when operating such an evaporator can be expanded.
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    According to a preferred further development of an embodiment of a fuel cell system according to the invention, it can further be provided that the first burner exhaust gas branch downstream of the first heat exchanger element and the second burner exhaust gas branch downstream of the second heat exchanger element are combined in a common burner exhaust gas branch, that the useful exhaust gas section has a first useful exhaust gas branch and a second useful exhaust gas branch divides into a branch in the first useful exhaust branch and the second useful exhaust branch, the first useful exhaust branch opening into the exhaust burner and in particular comprising the first valve, and the evaporator being arranged on the burner exhaust branch and on the second useful exhaust branch. In this particularly preferred embodiment of a fuel cell system according to the invention, the combined burner exhaust gas from the first burner exhaust gas branch and the second burner exhaust gas branch, brought together in the burner exhaust gas branch, can thus be fed to the evaporator. At the same time, the useful exhaust gas section is divided into a first useful exhaust gas branch and a second useful exhaust gas branch, in particular the second useful exhaust gas branch being fed directly to the evaporator. In particular, since the burner exhaust gas has already emitted at least part of its thermal energy after flowing through the two heat exchanger elements, the combined burner exhaust gas can be warmed up and, since the evaporator is preferably designed as a two-stage evaporator, the useful exhaust gas of the second useful exhaust branch can then be evaporated completely of the at least partially gaseous fluid can be used in the evaporator. A particularly efficient use of the total thermal energy in the fluids, in particular in the burner exhaust gas and in the useful exhaust gas, of a fuel cell stack according to the invention can be provided in this way.
    A fuel cell system according to the invention can also be designed such that the fuel cell system has a recirculation section for feeding useful exhaust gas into the useful gas, the recirculation section connecting the useful exhaust gas section, in particular the second useful exhaust gas branch, to the useful gas supply section. Such a recirculation section can thus provide that unused useful gas which is in the useful exhaust gas can be reused. It is also possible to provide thermal energy stored in the useful exhaust gas in this way in the fuel cell system. An overall efficiency at / 37
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    Operation of a fuel cell system according to the invention, both with regard to the consumption of useful gas and with regard to thermal efficiency, can be provided in this way.
    A fuel cell system according to the invention can also be developed in such a way that the flow control means comprise a recirculation blower in the recirculation section for setting a quantity of the useful exhaust gas conveyed in the recirculation section. Such a recirculation blower can be used, in particular, to control or regulate a quantity of the recirculated useful exhaust gas. In this way, at least indirectly, a control or regulation of a heat return can be made possible by introducing the useful exhaust gas into the useful gas supply section.
    Furthermore, in a fuel cell system according to the invention it can be provided that a condensation device is arranged in the useful exhaust gas section, in particular in the second useful exhaust gas branch downstream of the evaporator, for separating water and / or useful gas from the useful exhaust gas. In other words, water and / or useful gas can thus be obtained from the useful exhaust gas in this way. Water or useful gas recovered in this way can be stored and / or used in the fuel cell system according to the invention. This also enables an increase in overall efficiency when operating a fuel cell system according to the invention.
    A fuel cell system according to the invention can particularly preferably be further developed such that the fuel cell system has an operating valve upstream of the condensation device, the fuel cell system being designed to generate electrical energy when the operating valve is closed and to generate useful gas when the operating valve is open. In other words, operation of the fuel cell system for power generation or for electrolysis can be set by means of such an operating valve, which is arranged in particular in the useful exhaust gas section, preferably in the second useful exhaust gas branch, and controls or regulates a supply of useful exhaust gas to the condensation device. When the operating valve is open, the fuel cell system according to the invention will therefore consume electrical energy in order to supply water and / or useful gas, for example one with hydrogen / 37
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    AVL List GmbH and / or carbon monoxide enriched gas mixture. When the operating valve is closed, however, useful gas and air are used to generate electrical energy in the fuel cell system according to the invention. Possible uses for a fuel cell system according to the invention can be provided in a variety of ways.
    According to a second aspect of the invention, the object is achieved by a method for operating a fuel cell system according to the first aspect of the invention. A method according to the invention is characterized by the following steps:
    a) determining a temperature requirement of the fuel cell system,
    b) triggering the flow control means for distributing a thermal energy stored in the useful exhaust gas and / or in the burner exhaust gas in the fuel cell system, based on the temperature requirement of the fuel cell system determined in step a).
    An inventive method according to the second aspect of the invention is carried out by an inventive fuel cell system according to the first aspect of the invention. All of the advantages that have been described in detail in relation to a fuel cell system according to the invention according to the first aspect of the invention can thus also be provided by a method according to the invention for operating a fuel cell system, which is carried out by a fuel cell system according to the invention according to the first aspect of the invention.
    In a first step a) of a method according to the invention, a temperature control requirement of the fuel cell system is determined. In other words, after step a) of a method according to the invention has been carried out, information is available as to which temperature levels should prevail in the interior of the fuel cell system according to the invention in order to enable the fuel cell system to operate as efficiently as possible. At the same time, there is also information which deviations from these temperature levels to be set prevail. In addition, in step a) of a method according to the invention, it is also possible to determine the amounts of thermal energy in the fluids of the fuel cell system / 37
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    AVL List GmbH are stored, for example by a temperature measurement, for example on the exhaust air, the useful exhaust gas and / or the burner exhaust gas.
    This is used in the second step b) of a method according to the invention in order to control flow control means for distributing a thermal energy stored in the useful exhaust gas and / or burner exhaust gas in the fuel cell system. Since this control and distribution of the thermal energy is carried out, in particular based on the temperature requirement determined in step a), temperature levels are preferably established in the fuel cell system after carrying out a method according to the invention, which enable the most efficient operation of a fuel cell system according to the invention.
    In order to ensure this permanently, provision can in particular be made to carry out step a) and preferably also step b) of a method according to the invention continuously or at least essentially continuously.
    A method according to the invention can be developed in such a way that in step a) at least one local temperature control requirement of the fuel cell system is determined. Local in the sense of the invention can mean, in particular, locally broken down, for example with regard to the individual subunits and / or subsystems of the fuel cell system. A particularly need-adjusted temperature control requirement of the fuel cell system can be determined in this way.
    Furthermore, a method according to the invention can be designed such that, in step b), valves for controlling heat transport in the fuel cell system are switched as flow control means, in particular in order to meet a local temperature requirement determined in step a). Valves are particularly preferred flow control means, since they have a simple mechanical construction and are nevertheless designed quickly and effectively to control and / or regulate, in particular, an amount of fluid conveyed, each carrying thermal energy. Other possible flow control means can represent, for example, conveyor units, such as blowers, or heating elements. Overall, the flow control means, which can preferably be designed as valves, can be a particularly good one and in particular / 37
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    AVL List GmbH provides customized distribution of thermal energy that is stored in the fluids of the fuel cell system.
    Further measures improving the invention result from the following description of various exemplary embodiments of the invention, which are shown schematically in the figures. All of the features and / or advantages arising from the claims, the description and the figures, including structural details and spatial arrangements, can be essential to the invention both individually and in the various combinations. Elements with the same function and mode of operation are given the same reference numerals in FIGS. 1 to 4.
    Each shows schematically:
    FIG. 1 shows a first embodiment of a fuel cell system according to the invention,
    FIG. 2 shows a second embodiment of a fuel cell system according to the invention,
    Figure 3 shows a distribution system, and
    Figure 4 shows a method according to the invention.
    1 shows a possible embodiment of a fuel cell system 100 according to the invention. The fuel cell system 100 according to the invention in particular has a distribution system 40, as a result of which particularly efficient operation of the fuel cell system 100 according to the invention can be made possible. This is described below with reference to the shown embodiment of a fuel cell system 100 according to the invention.
    A fuel cell system 100 according to the invention in particular has a fuel cell stack 1, which can be constructed, for example, from a plurality of fuel cells, preferably solid fuel cells (SOFC). In particular, the fuel cell stack 1 has a first electrode 2 and a second electrode 3. The first electrode 2 is connected in particular to an air supply section 10, as a result of which air 30, for example taken from an environment 101 of the fuel cell system 100, can be supplied to the first electrode 2. Analog / 37
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    AVL List GmbH, the fuel cell system 100 has a useful gas supply section 11 through which the useful gas 31, for example hydrogen, carbon monoxide, methane or the like, can be supplied to the second electrode 3. In the fuel cell stack 1, in particular in the electrodes 2, 3, which are separated by an electrolyte in the fuel cell stack 1, the air 30 and the useful gas 31 can react with one another, for example by diffusing oxygen ions through the electrolyte, for example to generate electrical energy . This electrical energy can be delivered to an electrical connection 102, for example. Conversely, electrical energy can also be drawn from the electrical connection 102 in order to generate further or different useful gas 31 from air 30 and useful gas 31, for example water vapor and / or carbon dioxide, for example a gas mixture enriched with hydrogen and / or carbon monoxide. After the reactions in the fuel cell stack 1, the corresponding gases have to be derived again, for which purpose an exhaust air section 12 for discharging an exhaust air 32 and a useful exhaust gas section 13 for discharging a useful exhaust gas 33 are provided on the fuel cell stack 1. Both the exhaust air 32 and in particular the useful exhaust gas 33 are heated up by the reactions in the fuel cell stack 1. Basically, this depends on an operating point.
    The useful exhaust gas section 13 of the embodiment of a fuel cell stack 1 according to the invention shown in FIG. 1 is divided in a branch 14 into a first useful exhaust gas branch 15 and a second useful exhaust gas branch 16. The first useful exhaust gas branch 15 is fed to an exhaust gas burner 4, into which the exhaust air section 12 also opens. An at least partial catalytic combustion of the exhaust air 32 with the useful exhaust gas 33 in the exhaust gas burner 4 can thereby be provided. The resulting burner exhaust gas 34 in particular also has a particularly high temperature. However, high temperatures also mean a large amount of thermal energy stored in the fluids. In order to use the thermal energy of the burner exhaust gas 34 particularly effectively, the burner exhaust gas section 17 is divided into a first burner exhaust gas branch 18 and a second burner exhaust gas branch 19. The first burner exhaust gas branch 18 comprises in particular a first heat exchanger element 5 in the air supply section 10, by means of which the thermal energy is released to the Air 30, which is guided in the air supply section 10, is made possible. Correspondingly, the second exhaust burner branch 19 comprises a second heat exchanger element 6, which is arranged on the useful gas supply section 11. This second heat exchanger element 6 can also, for example, / 37
    PP31957AT
    AVL List GmbH to be trained as a reformer. A delivery of thermal energy directly to the useful gas 31 or a support for reforming the useful gas 31 can be provided in this way.
    Essential to the invention, as already described above, a fuel cell stack 1 according to the invention now has a distribution system 40. This distribution system 40 comprises, in particular, flow control means 50, by means of which a flow or a quantity of flowing fluids in the individual line sections 10, 13, 15, 16, 17, 18, 19, 20, 21 of the fuel cell stack 1 according to the invention is possible, which consequently also a control or regulation of the thermal energy provided by the respective fluids can be made possible. In order to determine a temperature requirement, in particular a local temperature requirement, of the fuel cell stack 1, the distribution system 40 also has sensor means 41, by means of which a temperature in the fuel cell stack 1 can be determined at four points, for example. These temperature measurements can be evaluated by an evaluation unit 42 and in particular compared with target values. A determination of a temperature requirement and information about the amounts of stored thermal energy stored in the fluids of the fuel cell system, in particular the useful exhaust gas 33 and the burner exhaust gas 34, can be provided in this way. The signal lines 43 required for signal transmission are not shown in FIG. 1. These signal lines 43 can be wired, but also wireless. The flow control means 50 are usually controlled via control lines 44, which are also not shown in FIG. 1. These control lines 44 can also be wired or wireless. Particularly preferably, a first valve 51 in the first useful exhaust gas branch 15, a second valve 52 in the first burner exhaust gas branch 18 and a third valve 53 in the second burner exhaust gas branch 19 can be used as flow control means 50. The first valve 51 can in particular be used to set an amount of useful exhaust gas 33 which is fed to the exhaust gas burner 4. A particularly simple setting of a combustion temperature in the exhaust gas burner 4 and thus an output temperature of the burner exhaust gas 34 can be provided in this way. The second valve 52 and third valve 53 in turn enable an amount of burner exhaust gas 34 to be set which is supplied to the first heat exchanger element 5 and the second heat exchanger element 6, respectively. A specially adapted supply, in particular also of thermal energy, to the heat exchanger elements / 37
    PP31957AT
    AVL List GmbH
    5, 6 can be made possible in this way. Another possible embodiment of a flow control means 50 can be an air supply fan 56. This air supply fan 56 controls the amount of air 30 that is extracted from an environment 101 and supplied to the fuel cell stack 1. For example, this air 30 can be supplied directly to the first electrode 2 of the fuel cell stack 1 via the air supply section 10. This amount can be further adjusted by an air valve 80. Furthermore, as also shown, a burner air supply 21 can be provided, which preferably branches off from the air supply section 10. A direct air supply of air 30 to the exhaust gas burner 4 can be made possible in this way, in particular in order to prevent or reduce an excessively high exhaust gas burner temperature. An additional fourth valve 54 or a heating element 55 as flow control means 50 in turn enable a particularly precise setting of the exhaust gas burner temperature, the air supply fan 56 also having a share in this control.
    In the illustrated embodiment of a fuel cell stack 1 according to the invention, a two-stage evaporator 7 is further arranged downstream on the second useful exhaust branch 16 and on the burner exhaust branch 20 after the first burner exhaust branch 18 and the second burner exhaust branch 19 have been merged again. The thermal energy required in the evaporator 7 can also be supplied and controlled by a distribution system 40 according to the invention, in particular by the first valve 51, the second valve 52 and the third valve 53. By means of different temperature levels of the burner exhaust gas 34, in particular according to the two heat exchanger elements 5, 6, and the useful exhaust gas 33 in the second useful exhaust gas branch 16 can in particular be provided that the supplied water 63 is heated in the first stage of the two-stage evaporator 7 and completely evaporated in the second stage. The evaporated water 63 is then fed to the useful gas feed section 11. In the process gas supply section 11, process gas 31, which either comes from a process gas tank 72 or from process gas sources 73, is guided, controlled by a process gas valve 81. The useful gas tank 72 in turn can be filled in particular by a fuel cell stack 1 which is operated in an electrolysis mode. For this purpose, the operating valve 8 is opened and the useful exhaust gas 33 is fed to a condensation device 9. In this condensation device 9, water 63 and condensate gas 35 are separated from the useful exhaust gas 33. A / 37
    PP31957AT
    AVL List GmbH
    Condensate gas aftertreatment 70 enables the condensate gas 35 to be cleaned, a condensate blower 71, which can also be operated as a compressor, enables conveying and / or compression and / or even liquefaction of the condensate gas 35. Particularly good storage of the condensate gas 35 as future useful gas 31 can take place in the useful gas tank 72 in this way. The water 63 separated in the condensation device 9 is fed to a water tank 60, which can also be filled with water 63 from other sources. A water pump 61 in turn then supplies the water 63 to the evaporator 7, regulated and controlled via a water valve 62.
    Overall, in a fuel cell stack 1 according to the invention, which has a distribution system 40, a particularly good and needs-adjusted distribution of thermal energy can be provided inside the fuel cell stack 1. A particularly efficient operation of a fuel cell system 100 according to the invention can be provided in this way.
    FIG. 2 shows a further possible embodiment of a fuel cell system 100 according to the invention. The fuel cell system 100 according to FIG. 2 differs from the fuel cell system 100 that was shown in FIG. 1 in that a recirculation section 22 is provided which additionally includes the useful exhaust gas section 13, in particular connects the second useful exhaust gas branch 16 to the useful gas supply section 11. A reuse of useful exhaust gas 33, in particular unreacted parts of useful gas 31 in the useful exhaust gas 33, can be provided in this way. In addition, the thermal energy stored in the useful exhaust gas 33, which is still present even after passing through the evaporator 7, can be returned to the operation of the fuel cell stack 1, as a result of which a renewed increase in efficiency can be provided. In the recirculation section 22, in particular, a recirculation blower 57 is also provided as flow control means 50 of a distribution system 40 according to the invention, so that a quantity of recirculated useful exhaust gas 33 can be controlled and / or regulated. With regard to all further components of the illustrated fuel cell system 100, reference is made to the detailed description with regard to FIG. 1.
    3 schematically shows a distribution system 40 as used in a fuel cell system 100 according to the invention (not shown) / 37
    PP31957AT
    AVL List GmbH can be. The distribution system 40 has in particular an evaluation unit 42, which is connected to sensor means 41 via signal lines 43 and to flow control means 50 via control lines 44. The signal lines 43 and control lines 44 are shown in FIG. 3 as physical lines, but can also be designed wirelessly. The sensor means 41, which are arranged at corresponding locations in the fuel cell stack 1 (not shown) of the fuel cell system 100, determine a current temperature at these points. The evaluation unit 42 uses this to generate a temperature control requirement, for example by comparing it with target values. At the same time, the sensor means 41 can also provide information as to which thermal energy is stored in the individual fluids of the fuel cell system 100. This can also be evaluated by the evaluation unit 42 and used in particular for controlling the flow control means 50, which can be designed, for example, as valves 51, 52, 53, as a fan 56 or as a heating element 55. Overall, a distribution system 40 according to the invention can thus provide a particularly good and needs-adjusted distribution of thermal energy in the fuel cell stack 1 of a fuel cell system 100 according to the invention. A particularly efficient and in particular self-contained operation, preferably self-sufficient operation, of a fuel cell system 100 according to the invention can be provided in this way.
    4 shows, in particular, a method according to the invention, as can be carried out by a fuel cell system 100 according to the invention (not shown). The elements necessary for executing the method are not shown in each case. Steps a) and b) are designated A and B in FIG. 4.
    In the first step a) of a method according to the invention, a temperature requirement of the fuel cell system 100 is determined. This temperature control requirement can preferably be a local temperature control requirement, in other words, a temperature control requirement assigned to locally resolved or subunits and / or subsystems of the fuel cell system 100. In other words, after step a) of a method according to the invention has been carried out, information is available as to which locations of the fuel cell system 100 there is a need for temperature control and to what extent.
    / 37
    PP31957AT
    AVL List GmbH
    This is used in the next step b) in order to control flow control means 50, for example valves 51, 52, 53, 54, in order to control or regulate a heat transport in the fuel cell system 100 in such a way that the temperature requirement determined in step a) can be met . Further flow control means 50, such as blowers 56, 57 or heating elements 55, can also be used in step b). After carrying out a method according to the invention, all the temperature control requirements in the fuel cell system 100 can thus preferably be satisfied, and thus a particularly efficient overall operation of a fuel cell system 100 according to the invention can be provided.
    / 37
    PP31957AT
    AVL List GmbH
    Reference list
    Fuel cell stack first electrode second electrode
    Exhaust burner first heat exchanger element second heat exchanger element evaporator
    Operating valve condensation device air supply section useful gas supply section exhaust air section useful exhaust gas branch branch first useful exhaust gas branch second useful exhaust gas branch burner exhaust gas section first burner exhaust gas branch second burner exhaust gas branch burner exhaust gas branch burner air supply recirculation section air
    Useful gas
    Exhaust air
    Useful exhaust
    Burner exhaust
    Condensate gas distribution system sensor means
    Evaluation unit
    Signal line control line
    Flow Control Means / 37
    PP31957AT
    AVL List GmbH first valve second valve third valve fourth valve heating element air supply fan recirculation fan
    Water tank water pump water valve water
    Condensate gas aftertreatment condensate blower
    Commercial gas tank Commercial gas source Air valve
    Commercial gas valve fuel cell system
    Environment electrical connection
    权利要求:
    Claims (17)
    [1]
    Claims
    1. A fuel cell system (100), comprising at least one fuel cell stack (1) with a first electrode (2) and a second electrode (3), an air supply section (10) for supplying air (30) to the first electrode (2), and a useful gas supply section (11) for supplying useful gas (31) to the second electrode (3), an exhaust air section (12) for removing exhaust air (32) from the first electrode (2), a useful exhaust gas section (13) for removing useful exhaust gas (33) from the second electrode (3), the exhaust air section (12) and the useful exhaust gas section (13) opening into an exhaust gas burner (4) for at least partially catalytic combustion of the exhaust air (32) and the useful exhaust gas (33), and a burner exhaust gas section (17) a first burner exhaust branch (18) and a second burner exhaust branch (19) for discharging burner exhaust gas (34) from the exhaust burner (4), the first burner exhaust branch (18) with a first heat exchanger element (5) in the air supply section (10) for already heat energy to the air (30) in the air supply section (10) and the second burner exhaust branch (19) is connected to a second heat exchanger element (6) in the useful gas supply section (11) for providing thermal energy to the useful gas (31) in the useful gas supply section (11) .
    characterized in that the fuel cell system (100) has a distribution system (40) with flow control means (50) at least in the useful exhaust gas section (13) and in the burner exhaust gas section (17) for distributing thermal energy stored in the useful exhaust gas (33) and / or in the burner exhaust gas (34) Has fuel cell system (100).
    [2]
    2. The fuel cell system (100) according to claim 1, characterized in that the distribution system (40) has sensor means (41) and an evaluation unit (42) for determining a temperature requirement of the fuel cell system (100).
    [3]
    3. Fuel cell system (100) according to one of the preceding claims, characterized in that the flow control means (50) at least one controllable first valve (51)
    26/37
    PP31957AT
    AVL List GmbH in the useful exhaust gas section (13), a controllable second valve (52) in the first burner exhaust branch (18) and a controllable third valve (53) in the second burner exhaust branch (19).
    [4]
    4. Fuel cell system (100) according to claim 3, characterized in that the second valve (52) in the first burner exhaust branch (18) is arranged downstream of the first heat exchanger element (5) and / or that the third valve (53) in the second burner exhaust branch (19 ) is arranged downstream of the second heat exchanger element (6).
    [5]
    5. The fuel cell system (100) according to any one of the preceding claims, characterized in that the fuel cell system (100) has, in particular from the air supply section (10) branching, burner air supply (21), the burner air supply (21) opening into the exhaust gas burner (4) .
    [6]
    6. The fuel cell system (100) according to claim 5, characterized in that the flow control means (50) has a fourth valve (54) for adjusting a quantity of the air (30) conveyed in the burner air supply (21) and / or a heating element (55) in the burner air supply (21) for heating the air (30) conveyed in the burner air supply (21).
    [7]
    7. The fuel cell system (100) according to one of the preceding claims, characterized in that the flow control means (50) comprise an air supply fan (56) in the air supply section (10) for adjusting a quantity of the air (30) conveyed in the air supply section (10).
    [8]
    8. The fuel cell system (100) according to one of the preceding claims, characterized in that the fuel cell system (100) has an evaporator (7) for providing water vapor for introduction into the useful gas supply section (11), the evaporator (7) for transmitting an im Useful exhaust gas (33) and / or thermal energy stored in the burner exhaust gas (34) downstream at the useful exhaust gas section (13) and / or downstream at the first burner exhaust gas branch
    27/37
    PP31957AT
    AVL List GmbH (18) and / or downstream on the second burner exhaust branch (19) is arranged.
    [9]
    9. The fuel cell system (100) according to claim 8, characterized in that the evaporator (7) is designed as a two-stage evaporator (7).
    [10]
    10. The fuel cell system (100) according to claim 9, characterized in that the first burner exhaust branch (18) downstream of the first heat exchanger element (5) and the second burner exhaust branch (19) downstream of the second heat exchanger element (6) are brought together in a common burner exhaust branch (20) that the useful exhaust gas section (13) has a first useful exhaust gas branch (15) and a second useful exhaust gas branch (16) and divides at a branching point (14) into the first useful exhaust gas branch (15) and the second useful exhaust gas branch (16), the first useful exhaust gas branch ( 15) opens into the exhaust burner (4) and in particular includes the first valve (51), and the evaporator (7) is arranged on the burner exhaust branch (20) and on the second useful exhaust branch (16).
    [11]
    11. The fuel cell system (100) according to one of the preceding claims, characterized in that the fuel cell system (100) has a recirculation section (22) for feeding useful exhaust gas (33) into the useful gas (31), the recirculation section (22) comprising the useful exhaust gas section ( 13), in particular the second useful exhaust gas branch (16), connects to the useful gas supply section (11).
    [12]
    12. The fuel cell system (100) according to claim 11, characterized in that the flow control means (50) comprise a recirculation fan (57) in the recirculation section (22) for adjusting an amount of the useful exhaust gas (33) conveyed in the recirculation section (22).
    [13]
    13. Fuel cell system (100) according to any one of the preceding claims, characterized in that in the useful exhaust gas section (13), in particular in the second useful exhaust gas branch (16) downstream of the evaporator (7), a condensation device (9)
    28/37
    PP31957AT
    AVL List GmbH is arranged to separate water and / or useful gas (31) from the useful exhaust gas (33).
    [14]
    14. The fuel cell system (100) according to claim 13, characterized in that the fuel cell system (100) upstream of the condensation device (9) has an operating valve (8), the fuel cell system (100) when the operating valve (8) is closed to generate electrical energy and is designed to generate useful gas (31) when the operating valve (8) is open.
    [15]
    15. A method for operating a fuel cell system (100) according to one of the preceding claims, characterized by the following steps:
    a) determining a temperature requirement of the fuel cell system (100),
    b) controlling the flow control means (50) to distribute a thermal energy stored in the useful exhaust gas (33) and / or in the burner exhaust gas (34) in the fuel cell system (100), based on the temperature requirement of the fuel cell system (100) determined in step a).
    [16]
    16. The method according to claim 15, characterized in that in step a) at least one local temperature requirement of the fuel cell system (100) is determined.
    [17]
    17. The method according to any one of claims 15 or 16, characterized in that in step b) as flow control means (50) valves (51, 52, 53, 54) for controlling a heat transfer in the fuel cell system (100) are switched, in particular by a Step a) to meet the determined local temperature requirements.
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    同族专利:
    公开号 | 公开日
    WO2019210346A3|2020-01-02|
    WO2019210346A2|2019-11-07|
    DE112019002272A5|2021-01-14|
    AT521207B1|2020-03-15|
    引用文献:
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    EP3020088B1|2013-07-09|2017-08-09|Ceres Intellectual Property Company Limited|Improved fuel cell systems and methods|
    US20160126570A1|2014-10-30|2016-05-05|Mitsubishi Hitachi Power Systems, Ltd.|Combined power generation system and unit, method, and program for controlling the same|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50372/2018A|AT521207B1|2018-05-03|2018-05-03|Fuel cell system and method for operating a fuel cell system|ATA50372/2018A| AT521207B1|2018-05-03|2018-05-03|Fuel cell system and method for operating a fuel cell system|
    PCT/AT2019/060150| WO2019210346A2|2018-05-03|2019-05-03|Fuel cell system and method for operating said fuel cell system|
    DE112019002272.5T| DE112019002272A5|2018-05-03|2019-05-03|FUEL CELL SYSTEM AND METHOD OF OPERATING A FUEL CELL SYSTEM|
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