• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
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    • 专利摘要:
    The present invention relates to a method for heating a fuel cell system (100a) for a motor vehicle (1000), comprising a fuel cell stack (1) with an anode section (2) and a cathode section (3), at least one evaporator (4) for evaporating a fuel A water mixture, a reformer (5) for reforming the vaporized fuel-water mixture for use in the anode section (2) of the fuel cell stack (1), and at least one burner (6) for combusting a fuel-containing fluid, wherein the reformer (5 ) in particular downstream of the at least one evaporator (4) and the at least one burner (6) in particular upstream of the at least one evaporator (4) are arranged and the at least one burner (6) with the at least one evaporator (4), for supplying in the at least one burner (6) burned fuel-containing fluid from the at least one burner (6) to the at least one evaporator (4), is in fluid communication and upstream of the at least one evaporator (4) is a fuel-water mixture source (7) for providing a fuel-water mixture for the at least one evaporator (4) is arranged. Furthermore, the invention relates to such a fuel cell system (100a) and a motor vehicle (1000) with the fuel cell system (100a).
    公开号:AT520482A1
    申请号:T50845/2017
    申请日:2017-10-03
    公开日:2019-04-15
    发明作者:Vincent Lawlor Dr
    申请人:Avl List Gmbh；
    IPC主号:
    专利说明:

    Process for rapid heating of a fuel cell system
    The present invention relates to a method for heating a fuel cell system, a fuel cell system, in particular an SOFC system, and a motor vehicle with a fuel cell system.
    Fuel cell systems usually have to be brought to operating temperature before they can be used to generate electricity. When starting a fuel cell system, care must be taken to ensure that an anode section does not come into contact with oxygen, or only as little as possible, since this can damage the anode section and lead to a corresponding functional impairment of the fuel cell system. In order to prevent oxygen at the anode section during the starting of the fuel cell system, as is known, for example, from US 2010/0203405 A1, the anode section is rinsed with water during the starting of the fuel cell system. To achieve this, either a specially designed water tank or a complex water recovery system is installed in the fuel cell system, which recovers water from exhaust gas from a fuel cell stack. Both solutions have proven unsatisfactory in practice.
    The object of the present invention is to at least partially take into account the problems described above. In particular, it is an object of the present invention to provide a fuel cell system, a motor vehicle and a method by means of which or in which a rapid heating of the fuel cell system or selected functional components of the fuel cell system can be implemented in a reliable and, in particular, protecting the anode section.
    The above object is solved by the claims. In particular, the above object is achieved by the method according to claim 1, the fuel cell system according to claim 14 and the motor vehicle according to claim 29. Further advantages of the invention result from the subclaims, the description and the drawings. Features and details that are described in connection with the method apply here, of course, also in connection with the fuel cell system according to the invention, the motor vehicle according to the invention and vice versa, so that with respect to Offenba / 47
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    AVL List GmbH is always or can be mutually referenced to the individual aspects of the invention.
    According to a first aspect of the present invention, a method for heating a fuel cell system is proposed. The fuel cell system has a fuel cell stack with an anode section and a cathode section, at least one evaporator for evaporating a fuel-water mixture, a reformer for reforming the evaporated fuel-water mixture for use in the anode section of the fuel cell stack, and at least one burner for burning a fuel-containing fluid , The reformer is preferably arranged downstream of the at least one evaporator and the at least one burner is preferably arranged upstream of the at least one evaporator. The at least one burner is in fluid communication with the at least one evaporator for supplying fuel-containing fluid burned in the at least one burner from the at least one burner to the at least one evaporator. A fuel-water mixture source for providing a fuel-water mixture for the at least one evaporator is arranged upstream of the at least one evaporator.
    The process has the following steps:
    Heating the at least one evaporator and / or a fluid within the at least one evaporator to a desired temperature or above,
    Supplying the fuel-water mixture from the fuel-water mixture source to the at least one evaporator as soon as the at least one evaporator has reached the target temperature or the temperature is above it,
    Feeding a fuel-water mixture evaporated by the at least one evaporator from the at least one evaporator that has reached or has reached the desired temperature to the reformer for reforming the evaporated fuel-water mixture, and / 47
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    - Feeding the reformed fuel-water mixture to the anode section, which is in a deactivated operating state, in which no current is generated by the fuel cell stack.
    The method according to the invention enables the fuel cell system, in particular the at least one evaporator and the reformer and the anode section, to be heated up while the reformed fuel-water mixture is applied to the anode section and thereby reliably protected against oxygen or at least against excessive oxygenation can. At the same time, the fuel cell stack, in particular the anode section, is heated. The fuel cell system can also be quickly heated by conveying the heated and vaporized fuel-water mixture from the fuel-water mixture source to the anode section.
    The target temperature depends in particular on the amount of liquid fuel or liquid water-fuel mixture that is evaporated or can be evaporated.
    A carbon-containing fuel, for example methane, is preferably used as fuel in the fuel-water mixture. The fuel can also be formed from a premixed ethanol-water mixture. Alternatively, two containers for water and ethanol can also be provided, the two fuel components being mixed with one another at a later point in time. In this case, the fuel-water mixture can be reformed into or on the reformer into methane, hydrogen, carbon monoxide and carbon dioxide. After the reformation process, there is particularly preferably only more hydrogen and methane. These substances are generally unproblematic on or in the anode section and can be burned, for example, in an exhaust gas burner or afterburner or by coated components. In particular, hydrogen and methane can also be used downstream of the anode section, which, as described above, is configured to temporarily generate no electricity, for further heating of the fuel cell system or selected system components of the fuel cell system.
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    The method is configured in particular for heating an SOFC system.
    The fuel-water mixture source can have one or more fuel-water mixture stores or be designed as such.
    The evaporator can be heated or heated by a heating device. The heating device can have an electrical heating means and / or an oxidative heating means.
    It can also be favorable if the reformer and / or the evaporator are mechanically connected to the burner, so that the reformer and / or the evaporator are heated or can be heated by the burner via heat conduction. This further improves the efficiency of the heating process of the components of the fuel cell system. The burner can also be designed with the reformer and / or with the evaporator as a (multi-stage) integral component. There is no need for a catalytic coating for an exothermic reaction of the reformer or the evaporator.
    The supply of fluids from one system component of the fuel cell system to another system component of the fuel cell system is to be understood to mean the delivery of the respective fluid from one system component into or to the other system component. If the fuel-water mixture is led, for example, from the fuel-water mixture source to the at least one evaporator, the fuel-water mixture can enter the at least one evaporator or the at least one evaporator, for example thermally interacting with the at least one an evaporator around the at least one evaporator. Suitable conveying devices are designed in the fuel cell system for guiding or conveying the respective fluids. Furthermore, the individual components of the fuel cell system are in contact with one another in such a way that thermal energy can be transferred to one another. In particular, the fluids are vaporized and exothermic reactions take place, so that the components can either be heated and / or kept at a desired temperature.
    By feeding the fuel-water mixture from the fuel-water mixture source to the at least one evaporator is to be understood that the fuel-water mixture from the fuel-water mixture source to the / 47
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    AVL List GmbH is at least partially supplied to at least one evaporator. By feeding the fuel-water mixture evaporated by the at least one evaporator from the at least one evaporator to the reformer is to be understood that the fuel-water mixture evaporated by the at least one evaporator is at least partially led from the at least one evaporator to the reformer. Reforming the evaporated fuel-water mixture means that the evaporated fuel-water mixture is at least partially reformed.
    As soon as the fuel cell system or selected system components of the fuel cell system have reached a desired operating temperature, the fuel cell system and thus also the anode section are switched to an activated operating state in which electricity is generated using reformed hydrogen.
    The fact that a component according to the invention is arranged downstream or upstream of another component according to the invention means that the one component is arranged directly or indirectly, that is to say separated from one another by further functional components, upstream or downstream of the other component. With such an arrangement, a fluid connection between the respective components is also preferably configured. Additionally or alternatively, it is favorable if the individual components are mechanically connected to one another in order to enable heat transfer between them.
    According to a development of the present invention, it is possible that in a method the at least one burner is designed for burning anode exhaust gas from the anode section, cathode exhaust gas from the cathode section and / or fuel from a primary fuel source which is arranged upstream of the at least one burner , wherein the at least one burner is supplied with fuel from the primary fuel source and the fuel is burned in the at least one burner, and wherein the burned fuel from the at least one burner to the at least one evaporator, for heating the at least one evaporator and / or the Fluid is supplied within the at least one evaporator to the target temperature or above. The primary fuel source is required for an activated or current-generating operating state of the fuel cell system and leads the evaporator or
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    AVL List GmbH to the reformer to be reformed fuel. As a result, for the heating process of the fuel cell system with the primary fuel source according to the invention, a system component is used which is basically required anyway in the fuel cell system. Apart from a fluid connection between the fuel source and the burner for supplying the fuel to the burner, additional system components can therefore be dispensed with. As a result, the fuel cell system can be provided in a particularly compact manner. In addition, an inexpensive solution for heating the fuel cell system can be created. In the burner, which is designed as an exhaust gas burner or comprises an exhaust gas burner, in particular anode exhaust gas is burned from the anode section with the supply of cathode exhaust gas, which is essentially air, from the cathode section. In particular, the cathode exhaust gas comprises only air, whereas the anode exhaust gas does not comprise completely burned fuel. The exhaust gas burner is in particular an afterburner. The burner can also be designed such that it takes over the function of a starting burner.
    In a further step, the fuel / water mixture is advantageously fed to the burner after the fuel cell stack has been acted upon and / or heated, in particular the anode section. This fuel-water mixture is then burned in the burner. This can be done both in its function as an exhaust burner and in its function as a start burner. The mixture which is now at least partially burned is subsequently fed to the at least one evaporator or reformer. Alternatively, after the anode section has been heated up, the fuel / water mixture can also be passed directly (without an intermediate step via the burner) to an evaporator or to the reformer, the evaporator and / or the reformer having a catalytic coating for this purpose. This results in an endothermic reaction and heating of the evaporator and / or reformer is further accelerated.
    In addition, it is possible in a method according to the invention that the fuel is burned by means of an electrically activatable catalyst, in particular by means of an electrically heatable metal catalyst, and the catalyst is deactivated as soon as the target temperature has been reached or exceeded. By using the activatable and deactivatable catalyst and / 47
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    The burner can be operated particularly efficiently with the automatic switch-off. The catalyst can also be provided in a particularly space-saving manner.
    Furthermore, it is possible in a method according to the present invention that the reformed fuel-water mixture is led from the anode section to the at least one burner in which at least one burner is at least partially burned and the at least partially burned fuel-water mixture from that at least one burner is fed to the anode section via the at least one evaporator and the reformer. As a result, the flushing fluid used at the anode section, that is to say the evaporated and reformed fuel / water mixture, in particular the reformed, combustible components thereof, can be used in the burner in order to further heat up the evaporator.
    As a result, the heating of the evaporator and the reformer can not only be carried out safely but also particularly efficiently.
    It can be a further advantage if, in a method according to the invention, the fuel-water mixture is injected from the fuel-water mixture source through an injector into the at least one evaporator. The injector allows the fuel-water mixture to be injected into the at least one evaporator in a simple manner. This makes it easy to adjust the amount of fluid with which the anode section is to be rinsed when the fuel cell system is started. In addition, any temperature adjustments to the at least one evaporator or to the reformer can accordingly be made spontaneously and easily by adjusting an injection quantity of the reformed fuel-water mixture that is burned by the burner by a desired injection process of the injector.
    In a method according to the present invention, it is also possible for the reformer to be supplied with air or another oxygen-containing fluid before the reforming or during the reforming of the evaporated fuel-water mixture. By supplying air or an oxygen-containing fluid, an exothermic reaction in the reformer can be promoted, in which even more heat can be generated in the reformer and in the anode section. As a result, the fuel cell system can be heated particularly quickly. The air can be supplied from an air source, for example a compressed air tank, or preferably from a blower. The blower is preferably the blower that sends air to the Katho / 47
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    AVL List GmbH leads the section. In this case, the air can be branched off into the reformer from a fluid line which is configured between the blower and the cathode section.
    In addition, it can be advantageous in a method according to the invention if the reformer is preheated before the vaporized fuel-water mixture is fed to the reformer. The desired reforming reaction can take place particularly reliably in a preheated reformer. Unwanted reforming products that could arise from a non-preheated reformer can be prevented. As a result, the method can be operated in a particularly stable and reliable manner. For example, the reformer can be mechanically connected to the burner for this purpose and can be heated by heat conduction from the burner to the reformer by the heat of the burner.
    Experiments within the scope of the present invention have shown that it is advantageous if the target temperature is at least 250 ° C., in particular at least 300 ° C. That is, the at least one evaporator and / or the fluid within the at least one evaporator are heated to at least 250 ° C., in particular at least 300 ° C., before the fuel-water mixture from the fuel-water mixture source to the at least one Evaporator guided or injected into it. This temperature range has proven to be sufficiently high to vaporize the fuel-water mixture as desired.
    According to a further embodiment variant of the present invention, it is possible that the fuel-water mixture evaporated by the at least one evaporator is at least partially from the at least one evaporator that has reached the target temperature or whose temperature is higher than the fuel-containing fluid to the at least one a burner is led. By using the vaporized fuel-water mixture, fuel from the fuel source can be saved or, depending on the application, a particularly large and simple amount of fuel can be provided on the burner. This allows the burner and thus also the evaporator and the reformer to be brought to the desired temperature quickly and easily. The fact that the fuel-water mixture is to be regarded as the fuel-containing fluid means in particular that the fuel-water mixture is used at least as part of the fuel-containing fluid supplied to the burner.
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    It is also possible that, in a method according to the invention, the fuel-water mixture evaporated by the at least one evaporator for heating the fuel-water mixture is led to the at least one burner on or in a heat exchange section of the at least one burner. In this case, the vaporized fuel-water mixture is guided in particular in a fluid channel which is arranged at least in sections along the burner, preferably adjacent to it, to an inlet section for admitting the fuel-water mixture into the burner. This allows heat, which is generated in the burner, to be transferred to the fuel-water mixture in a simple, effective and efficient manner, as a result of which it can be introduced into the burner in a preheated and / or further evaporated manner. As a result, the burner can be heated even more quickly, which in turn means that the fuel / water mixture which is fed into the at least one burner via the heat exchange section can be heated even more. The teaching in question can therefore create a particularly efficient and effective heating circuit.
    Furthermore, in a method according to the present invention, it is possible for a fuel source for providing a fuel for the at least one evaporator to be arranged upstream of the at least one evaporator, fuel evaporated by the at least one evaporator for heating the fuel at or in a heat exchange section of the at least one burner as the fuel-containing fluid is led to the at least one burner. That is, in addition or as an alternative to the fuel-water mixture source, a separate fuel source is arranged, in which case, too, heat generated in the burner can be transferred to the fuel in a simple, effective and efficient manner. As a result, the fuel can already be preheated and / or vaporized and introduced into the burner. This in turn allows the burner to be heated particularly quickly, as a result of which the fuel which is fed into the at least one burner via the heat exchange section can also be heated even more. In a preferred embodiment, in addition to the fuel source mentioned above, the fuel-water mixture source is also arranged, by means of which fuel evaporated via a separate evaporator for evaporating the fuel-water mixture, which is arranged in series with the evaporator for the fuel source -Water mixture to the reformer / 47
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    AVL List GmbH is fed. In this case, the two evaporators are each designed as two-way systems, which are relatively inexpensive to provide.
    In addition, in a method according to the present invention, it is possible for the fuel-water mixture and / or the fuel in each case by an intermediate heating device, in particular an electrical intermediate heating device, which is located downstream of the fuel-water mixture source or the fuel source and is arranged upstream of the at least one burner, is heated until the fuel-water mixture or the fuel has reached a predefined temperature or the temperature is above it. Using the intermediate heating device, the heating or preheating of the burner by the fuel from the primary fuel source mentioned at the beginning can be dispensed with. As a result, it is also possible to dispense with a line system required for this, which would generally require more installation space than the intermediate heating device and a higher degree of complexity in the fuel cell system. Accordingly, the fuel cell system can be provided in a correspondingly simple and compact manner using the intermediate heating device according to the invention. The intermediate heating device can be arranged upstream of the evaporator and / or downstream of the evaporator.
    It can be a further advantage if the intermediate heating device is deactivated in a method according to the invention as soon as the at least one burner, a fluid in the at least one burner, the at least one evaporator and / or a fluid in the at least one evaporator have reached a predefined temperature or the temperature is above. As soon as the respective predefined temperature is reached, the intermediate heating device is no longer required. Due to the automatic shutdown, the fuel cell system can be operated in an energy-saving manner. In particular, it is advantageous if the components described above are mechanically connected to one another in such a way that heat is conducted and transferred from the burner to the evaporator.
    According to a further aspect of the present invention, a fuel cell system for a motor vehicle is provided. The fuel cell system has a fuel cell stack with an anode section and a cathode section, at least one evaporator for evaporating a fuel water 11/47
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    Mixture, a reformer for reforming the vaporized fuel-water mixture for use in the anode section of the fuel cell stack, and at least one burner for burning a fuel-containing fluid. The reformer is arranged downstream of the at least one evaporator and the at least one burner is arranged upstream of the at least one evaporator. The at least one burner is in fluid communication with the at least one evaporator for supplying fuel-containing fluid burned in the at least one burner from the at least one burner to the at least one evaporator. A fuel-water mixture source for providing a fuel-water mixture for the at least one evaporator is arranged upstream of the at least one evaporator.
    A fuel cell system according to the invention thus has the same advantages as have been described in detail with reference to the method according to the invention. The fuel cell system is preferably designed as an SOFC system. In a further embodiment variant of the invention, the fuel cell system has a control unit that is configured and configured to carry out a method as described in detail above. The control unit is to be understood as a control and / or regulating unit for executing or activating the individual method steps.
    The fuel and water in the fuel-water mixture source are at least temporarily provided in liquid form. The fuel-water mixture source preferably has a fuel-water mixture store in which a premixed fuel-water mixture is stored in the liquid state. The fuel-water mixture is stored in a particularly simple and compact manner in the fuel cell system.
    In a further embodiment variant of the present invention, the at least one evaporator is preferably arranged directly downstream of the fuel-water mixture source. As a result, the dosage can be adjusted quickly and easily with regard to the fuel-water mixture for the at least one evaporator.
    In addition, in a fuel cell system according to the invention, it is possible for the at least one evaporator to be located directly downstream of the at least one / 47
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    Brenner is arranged. A particularly effective heat transfer from the burner to the at least one evaporator can thereby be ensured, as a result of which the fuel and / or the fuel / water mixture in or on the at least one evaporator can be evaporated correspondingly effectively.
    It is particularly advantageous if, in the fuel cell system according to the invention, the at least one evaporator and / or the reformer are connected directly to the at least one burner. Thus, the evaporator and / or the reformer are mechanically connected to the burner, as a result of which heat can be thermally transferred from the burner to the evaporator or reformer via heat conduction. In this embodiment, therefore, no catalytic coatings of the evaporator and / or the reformer are necessary. There is no need for exothermic reactions to provide heat. For example, the evaporator can be arranged directly after the burner or enclosing it. It is always advantageous if the components are arranged with respect to one another in such a way that as much heat as possible is thermally conducted from the burner to the reformer and / or evaporator. In the context of the invention, the fact that the at least one evaporator and / or the reformer are connected directly to the at least one burner means that these components connect directly to one another and are not arranged at a distance from one another; they are physically connected.
    In the present case, the at least one burner has in particular an exhaust gas burner and / or a starting burner. The starting burner is designed in particular upstream of the exhaust burner, preferably directly upstream of the exhaust burner, and particularly preferably integrally connected to the exhaust burner. At least the exhaust gas burner, but generally also the start burner, are required anyway in an SOFC system according to the invention, which is why no new or separate functional unit is required for the burner. The fuel cell system can accordingly be made compact and simple.
    In a fuel cell system according to the invention, an air supply device, in particular a blower, for supplying air to the reformer can be arranged before the reforming or during the reforming of the evaporated fuel-water mixture. The air supply device is preferably already used for supplying air or an oxygen-containing fluid to the cathode section / 47
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    AVL List GmbH required. That is, a functional component of the fuel cell system can be used that is required in the fuel cell system anyway. As a result, the fuel cell system can be made available compactly and inexpensively.
    Alternatively or additionally, it is advantageous if a further air supply device is provided, which supplies air downstream of the reformer. This triggers an endothermic, partial oxidation reaction in the anode, which also accelerates a heating process. An anode temperature for the oxidation reaction should be higher than 250 ° C, especially higher than 300 ° C. It is always important that all of the oxygen in the anode is burned to avoid reoxidation at the anode. This is achieved when a so-called rich combustion takes place, i.e. when the lambda value is less than 1 (more fuel than air; lack of air).
    Furthermore, in a fuel cell system according to the present invention, it is possible for the at least one burner to be configured for burning anode exhaust gas from the anode section, cathode exhaust gas from the cathode section and / or fuel from a fuel source which is arranged upstream of the at least one burner wherein the fuel source is configured to supply the fuel to the at least one burner, and the at least one burner for supplying the burned fuel from the at least one burner to the at least one evaporator, to heat the at least one evaporator and / or the fluid within of the at least one evaporator to the target temperature or above.
    Furthermore, the at least one burner can have an electrically activatable catalytic converter, in particular an electrically heated metal catalytic converter, for burning the fuel, the catalytic converter being configured to be deactivated as soon as the desired temperature is reached or exceeded. Downstream of the fuel-water mixture source and upstream of the at least one evaporator, at least one injector for injecting the fuel-water mixture from the fuel-water mixture source into the at least one evaporator can be arranged. A heat exchange section can be configured on an outer wall section of the at least one burner, on or in which the fuel-water mixture evaporated by the at least one evaporator can be fed to the at least one burner. Upstream of the at least one evaporator can / 47
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    AVL List GmbH a fuel source for providing a fuel for the at least one evaporator can be arranged, wherein fuel evaporated by the at least one evaporator for heating the fuel on or in a heat exchange section of the at least one burner as the fuel-containing fluid can be guided to the at least one burner. An intermediate heating device, in particular an electrical intermediate heating device, for heating the fuel / water mixture or the fuel can be arranged downstream of the fuel / water mixture source and / or the fuel source and upstream of the at least one burner, the intermediate heating device being configured to be the fuel -Heating the water mixture or the fuel until the fuel-water mixture or the fuel has reached a predefined temperature or the temperature is above it. The intermediate heating device can be configured to be deactivated as soon as the at least one burner, a fluid in the at least one burner, the at least one evaporator and / or a fluid in the at least one evaporator have reached a predefined temperature or the temperature is above it. The fuel cell system thus brings with it the same advantages as have been described in detail above with reference to the associated method according to the invention.
    According to a further aspect of the present invention, a motor vehicle with a fuel cell system as described above is provided. A motor vehicle according to the invention thus also has the advantages described above. The motor vehicle is preferably a car or an LWK.
    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 or the drawing, including structural details and spatial arrangements, can be essential to the invention both individually and in the various combinations.
    Each shows schematically:
    FIG. 1 shows a block diagram for illustrating a fuel cell system according to a first embodiment of the present invention, / 47
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    Figure 2 2 shows a partially sectioned side view of a section of the fuel cell system shown in FIG. 1, Figure 3 1 is a block diagram showing a fuel cell system according to a second embodiment of the present invention. Figure 4 1 is a block diagram showing a fuel cell system according to a third embodiment of the present invention. Figure 5 1 is a block diagram showing a fuel cell system according to a fourth embodiment of the present invention. Figure 6 1 is a block diagram showing a fuel cell system according to a fifth embodiment of the present invention. Figure 7 1 is a block diagram showing a fuel cell system according to a sixth embodiment of the present invention. Figure 8 1 is a block diagram showing a fuel cell system according to a seventh embodiment of the present invention. Figure 9 1 is a block diagram showing a fuel cell system according to an eighth embodiment of the present invention; Figure 10 1 is a block diagram showing a fuel cell system according to a ninth embodiment of the present invention. Figure 11 a motor vehicle with a fuel cell system according to the invention, Figure 12 4 shows a flowchart for explaining a method according to a first embodiment of the present invention, and Figure 13 a flowchart for explaining a method according to a second embodiment of the present invention.
    Elements with the same function and mode of operation are given the same reference numerals in FIGS. 1 to 13.
    1 schematically shows a fuel cell system 100a for a motor vehicle 1000 in the form of an SOFC system according to a first embodiment. The / 47
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    Fuel cell system 100a shows an anode section 2, an evaporator 4 for vaporizing a fuel-water mixture, a reformer 5 for reforming the vaporized fuel-water mixture for use in the anode section 2 and a burner 6 for burning one from a primary fuel source 14. The primary fuel source 14 is an optional preheating element such as a start burner.
    The reformer 5 is arranged downstream of the evaporator 4 and the burner 6 is arranged upstream of the evaporator 4. The burner 6 is in fluid connection with the evaporator 4, for supplying fuel burned in the burner 6 from the burner 6 to the evaporator 4, or is mechanically connected to the latter. A fuel-water mixture source 7 in the form of a fuel-water mixture store for providing a ready-mixed fuel-water mixture for the evaporator 4 is arranged directly upstream of the evaporator 4.
    The fuel and the water are provided in the fuel-water mixture source 7 in liquid form. The evaporator 4 is arranged directly downstream of the fuel-water mixture source 7. The evaporator 4 is also arranged directly downstream of the burner 6.
    An injector 12 for injecting the fuel-water mixture from the fuel-water mixture source 7 into the evaporator 4 is arranged downstream of the fuel-water mixture source 7 and thus upstream of the evaporator 4.
    A heat exchanger 8 is also arranged directly downstream of the reformer 4, via which burned exhaust gas from the burner 6 can be discharged into the surroundings 9 of the fuel cell system.
    The burner 6 is designed to supply the burned fuel from the burner 6 to the evaporator 4, to heat the evaporator 4 and the fluid within the evaporator 4 to a desired temperature or above. It is advantageously provided that the burner 6 is also physically connected to the evaporator 4, for example the evaporator 4 can be arranged directly downstream of the burner 6 or around the burner 6.
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    2, a portion of the fuel cell system 100a according to the first embodiment will be explained in detail. The burner 6 shown in FIG. 2 has an electrically heatable metal catalytic converter for burning the fuel, the catalytic converter being configured to be deactivated as soon as the target temperature is reached or exceeded. As shown in FIG. 2, the fuel-water mixture can be passed via the evaporator 4 to the reformer 5 and from there to the anode section 2. The reformer 5 is arranged in a ring around the burner 6 in the form of an exhaust gas burner. A preheating device 10 in the form of an electrical heating device for preheating fuel to be burned in the burner 6 is arranged upstream of the burner 6 directly on the burner 6.
    Further embodiments of the fuel cell system are described below with reference to FIGS. 1 to 10, only the respective distinguishing features between the embodiments being explained in each case. This is to avoid a redundant description if possible.
    FIG. 3 shows a fuel cell system 100b according to a second embodiment. In the fuel cell system 100b shown, a heat exchange section 18 is configured on an outer wall section of the burner 6, at which the fuel-water mixture evaporated by the evaporator 4 can be fed to the burner 6. In addition, the fuel-water mixture is passed from the fuel-water mixture source 7 to both the burner 6 and the reformer 5 in FIG. 3.
    4 shows a fuel cell system 100c according to a third embodiment. In the fuel cell system 100c shown, a fuel source 7a for providing a fuel for the first evaporator 4a is arranged upstream of a first evaporator 4a, fuel evaporated by the first evaporator 4a for heating the fuel on or in the heat exchange section 18 of the burner 6 as the fuel-containing fluid to the burner 6 is feasible. In addition, a fuel-water mixture source 7b for providing a fuel-water mixture for the second evaporator 4b is arranged upstream of a second evaporator 4b, wherein the fuel-water mixture evaporated by the second evaporator 4b can be conducted to the reformer 5. The second evaporator 4b is accordingly upstream of the reformer 5 at / 47
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    AVL List GmbH ordered. The first evaporator 4a and the second evaporator 4b are arranged in series with each other and upstream of the heat exchanger 8.
    FIG. 5 shows a fuel cell system 100d according to a fourth embodiment, which is similar to the fuel cell system 100c according to the third embodiment. In the fuel cell system 100d according to the fourth embodiment, the first evaporator 4a and the second evaporator 4b are arranged parallel to one another. This can be implemented for a particularly compact construction of the fuel cell system 100d.
    FIG. 6 shows a fuel cell system 100e according to a fifth embodiment. In the illustrated fuel cell system 100e, an electrical intermediate heating device 11 for heating the fuel-water mixture or the fuel is arranged downstream of the fuel-water mixture source 7, more precisely directly downstream of the evaporator 4, the intermediate heating device 11 being configured heating the fuel-water mixture until the fuel-water mixture has reached a predefined temperature or the temperature is above it. The intermediate heating device 11 is configured to be deactivated as soon as the burner 6 and / or a fluid in the burner have reached a predefined temperature or the temperature is above it. The predefined temperature can be, for example, approximately 650 ° C. A valve 20 is arranged downstream of the evaporator 4 and upstream of the reformer 5. In a closed position, the valve 20 prevents fuel or the water / fuel mixture from flowing into the reformer 5 without the latter being evaporated or being able to be evaporated. This prevents possible condensation of the water-fuel mixture in the reformer 5 and flooding of the reformer 5 with liquid fuel. The valve 20 can also be provided in all other embodiments of the invention.
    FIG. 7 shows a fuel cell system 100f according to a sixth embodiment. In the illustrated fuel cell system 100f, the intermediate heating device 11 is arranged downstream of the fuel-water mixture source and upstream of the evaporator 4.
    As shown in FIGS. 3 to 7, the injector 12 is in each case arranged relatively far from the burner 6 and is therefore good against the heat of the burner
    PP31603AT
    AVL List GmbH protects. Among other things, a standard injector can therefore be used as the injector 12, i.e. an injector which does not have to meet any particular requirements either in terms of its shape or in terms of temperature resistance.
    FIG. 8 shows a fuel cell system 100g according to a seventh embodiment. In the fuel cell system 100g shown, a fuel cell stack with the anode section 2 and a cathode section 3 is shown. In addition to the primary fuel source 14, a water source 15 and an air supply device 16 in the form of a fan are also shown. The blower is configured to supply air to the reformer 5 before reforming or during the reforming of the vaporized fuel-water mixture.
    9 shows a fuel cell system 100h according to an eighth embodiment. In the fuel cell system 100h shown, the burner has an exhaust burner 6 and a start burner 17, the start burner 17 being arranged upstream of the exhaust burner 6 directly thereon.
    FIG. 10 shows a fuel cell system 100i according to a ninth embodiment. In the fuel cell system 100i shown, a fluid line for supplying fuel from the primary fuel source 14 to the burner 6 was dispensed with, since the intermediate heating device 11 is arranged upstream of the evaporator 4.
    In all of the exemplary embodiments according to FIGS. 8 to 10, instead of the primary fuel source 14 and the water source 15, only a single fuel-water mixture tank with a premixed fuel-water mixture can also be provided. This fuel-water mixture tank can basically be designed like the fuel-water mixture source 7 and is arranged upstream of the evaporator 4.
    FIG. 11 shows a motor vehicle 1000 with a fuel cell system 100a according to the first embodiment. The motor vehicle 1000 furthermore has an electric motor 200 which can be driven by electrical energy from the fuel cell system 100a. The motor vehicle 1000 or the fuel cell system 100a shown in FIG. 11 has a control unit 19 which / 47
    PP31603AT
    AVL List GmbH is configured and designed to carry out a method as described in detail below.
    A method according to a first embodiment is subsequently explained with reference to FIGS. 12 and 1. In a first step S1, the evaporator 4 is heated by the burner 6 to a target temperature of approximately 300 ° C. Fuel in the burner 6 is burned by an electrically heatable metal catalytic converter, the catalytic converter being deactivated as soon as the target temperature is reached or is exceeded or has been exceeded.
    As soon as the evaporator 4 has reached the desired temperature or the temperature is above it, a fuel-water mixture is injected from the fuel-water mixture source 7 into the evaporator 4 by the injector 12 in a subsequent second step S2.
    Then, in a third step S3, the reformer 5 is supplied with a fuel-water mixture evaporated by the evaporator 4 from the evaporator 4, which has reached or has reached the desired temperature, so that the reformer reforms the evaporated fuel-water mixture can. Air is supplied to the reformer 5 before the reforming or during the reforming of the evaporated fuel-water mixture. In addition, the reformer 5 is preheated before the vaporized fuel-water mixture is fed to the reformer 5.
    Now the reformed fuel-water mixture is supplied to the anode section 2, which is in a deactivated operating state, in which no electricity is generated by the fuel cell stack, in a fourth step S4, whereby the anode section is rinsed during the starting and heating of the fuel cell system and is protected accordingly.
    The reformed fuel-water mixture can then be led or recirculated from the anode section 2 to the burner 6, at least partially burned in the burner 6 and the at least partially burned fuel-water mixture from the burner 6 via the evaporator 4 and the reformer 5 again are fed to the anode section 2. The corresponding heating circuit can now run until the fuel cell system is heated to the desired temperature.
    / 47
    PP31603AT
    AVL List GmbH
    A method according to a second embodiment is subsequently explained with reference to FIGS. 13 and 6. In a first step S1, the burner 6 is heated to a target temperature of approximately 300 ° C. by means of the electrically heatable metal catalyst. As soon as the target temperature has been reached, the metal catalyst is switched off.
    In a second step S2, a fuel-water mixture is fed to the burner 6 through the injector 12 via the evaporator 4, the electrical intermediate heating device 11 being activated and the fuel-water mixture being guided along the burner 6.
    As soon as the evaporator 4 has reached a predefined temperature at which the fuel-water mixture can be evaporated in the desired manner by the heat generated in the burner 6, the intermediate heating device 11 is deactivated in a third step S3. In the heating circuit now present, both the energization of the metal catalyst and the energization of the intermediate heating device can be dispensed with.
    In addition to the illustrated embodiments, the invention permits further design principles.
    Thus, as shown in FIGS. 4 and 5, it is possible for a fuel source 7a to provide fuel for the first evaporator 4a to be arranged upstream of the first evaporator 4a, fuel evaporated by the first evaporator 4a for heating the fuel at the heat exchange section 18 of the burner 6 as the fuel-containing fluid is led to the burner 6. That is, instead of the fuel-water mixture, the burner 6 can also be supplied with a different fuel mixture or a different fuel in a method according to FIG. 13.
    In addition, as shown in FIGS. 3, 6 and 7, it is possible that the fuel-water mixture evaporated by the evaporator 4 is at least partially from the evaporator 4 that has reached the desired temperature or its temperature lies above when the fuel-containing fluid is led to the burner 6. That is, the fuel-water mixture is partly led from the evaporator 4 to the burner 6 and partly to the reformer 5.
    / 47
    PP31603AT
    AVL List GmbH
    LIST OF REFERENCE NUMBERS
    Fuel cell stack Anode section Cathode section Evaporator Evaporator Evaporator Reformer Exhaust gas burner (burner) Fuel-water mixture source Fuel source
    Fuel-water mixture source
    heat exchangers
    Surroundings
    preheater
    Zwischenheizvorrichtung
    injector
    fuel source
    water source
    fan
    Start burner
    Heat exchange section
    control unit
    Valve
    The fuel cell system
    electric motor
    motor vehicle
    权利要求:
    Claims (29)
    [1]
    claims
    1. A method for heating a fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) comprising a fuel cell stack (1) with an anode section (2) and a cathode section (3), at least one evaporator (4 ; 4a, 4b) for evaporating a fuel-water mixture, a reformer (5) for reforming the evaporated fuel-water mixture for use in the anode section (2) of the fuel cell stack (1), and at least one burner (6, 17) for burning a Fuel-containing fluid, the reformer (5) preferably being arranged downstream of the at least one evaporator (4; 4a, 4b) and the at least one burner (6, 17) preferably being arranged upstream of the at least one evaporator (4; 4a, 4b) and the at least one a burner (6, 17) with the at least one evaporator (4; 4a, 4b) for supplying fuel-containing fluid burned in the at least one burner (6, 17) from the at least one burner (6, 17) to the whom at least one evaporator (4; 4a, 4b), is in fluid communication and upstream of the at least one evaporator (4; 4a, 4b) is a fuel-water mixture source (7; 7a, 7b) for providing a fuel-water mixture for the at least one evaporator ( 4; 4a, 4b), the method comprising the following steps:
    Heating the at least one evaporator (4; 4a, 4b) and / or a fluid within the at least one evaporator (4; 4a, 4b) to a target temperature or above,
    - Feeding the fuel-water mixture from the fuel-water mixture source (7; 7a, 7b) to the at least one evaporator (4; 4a, 4b) as soon as the at least one evaporator (4; 4a, 4b) reaches the desired temperature or the temperature is above
    - Feeding a fuel-water mixture vaporized by the at least one evaporator (4; 4a, 4b) from the at least one evaporator (4; 4a, 4b), which has reached the target temperature or whose temperature is above it, to the reformer (5) to reform the vaporized fuel-water mixture, and
    - Feeding the reformed fuel-water mixture to the anode section (2), which is in a deactivated operating state, in which no current is generated by the fuel cell stack.
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    [2]
    2. The method according to claim 1, characterized in that the at least one burner (6, 17) for burning anode exhaust gas from the anode section (2), cathode exhaust gas from the cathode section (3) and / or fuel from a fuel source (14) , which is arranged upstream of the at least one burner (6, 17), the at least one burner (6, 17) being supplied with fuel from the fuel source (14) and the fuel in the at least one burner (6, 17) is burned, and wherein the burned fuel from the at least one burner (6, 17) to the at least one evaporator (4; 4a, 4b), for heating the at least one evaporator (4; 4a, 4b) and / or the fluid inside of the at least one evaporator (4; 4a, 4b) to the target temperature or above.
    [3]
    3. The method according to claim 2, characterized in that the fuel is burned by means of an electrically activatable catalyst, in particular by means of an electrically heatable metal catalyst, and the catalyst is deactivated as soon as the target temperature is reached or exceeded.
    [4]
    4. The method according to any one of the preceding claims, characterized in that the reformed fuel-water mixture is guided from the anode section (2) to the at least one burner (6, 17), in the at least one burner (6, 17) at least is partially burned and the at least partially burned fuel-water mixture is fed from the at least one burner (6, 17) via the at least one evaporator (4) and the reformer (5) to the anode section (2).
    [5]
    5. The method according to any one of the preceding claims, characterized in that the fuel-water mixture from the fuel-water mixture source (7; 7a, 7b) through an injector (12) in the at least one evaporator (4; 4a , 4b) is injected.
    25/47
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    [6]
    6. The method according to any one of the preceding claims, characterized in that the reformer (5) before the reforming or during the reforming of the evaporated fuel-water mixture air is supplied.
    [7]
    7. The method according to any one of the preceding claims, characterized in that the reformer (5) is preheated to the reformer (5) before the vaporized fuel-water mixture is supplied.
    [8]
    8. The method according to any one of the preceding claims, characterized in that the target temperature is at least 250 ° C, in particular at least 300 ° C.
    [9]
    9. The method according to any one of the preceding claims, characterized in that the fuel-water mixture evaporated by the at least one evaporator (4; 4a, 4b) at least partially from the at least one evaporator (4; 4a, 4b), which has the desired temperature has reached or whose temperature is above when the fuel-containing fluid is led to the at least one burner (6, 17).
    [10]
    10. The method according to claim 9, characterized in that the fuel-water mixture evaporated by the at least one evaporator (4; 4a, 4b) for heating the fuel-water mixture on or in a heat exchange section (18) of the at least one burner (6 , 17) to which at least one burner (6, 17) is guided.
    [11]
    11. The method according to any one of the preceding claims, characterized in that a fuel source (7a) for providing a fuel for the at least one evaporator (4a) is arranged upstream of the at least one evaporator (4a), the at least one evaporator (4a) vaporized fuel for heating the fuel on or in a heat
    26/47
    PP31603AT
    AVL List GmbH exchange section (18) of the at least one burner (6, 17) as the fuel-containing fluid is led to the at least one burner (6, 17).
    [12]
    12. The method according to any one of claims 9 to 11, characterized in that the fuel-water mixture and / or the fuel in each case by an intermediate heating device (11), in particular an electrical intermediate heating device (11), which is downstream of the fuel-water mixture -Source (7; 7a, 7b) or the fuel source (7a) and upstream of the at least one burner (6, 17) is heated until the fuel-water mixture or the fuel has reached a predefined temperature or the temperature lies above.
    [13]
    13. The method according to claim 12, characterized in that the intermediate heating device (11) is deactivated as soon as the at least one burner (6, 17), a fluid in the at least one burner, the at least one evaporator (4; 4a, 4b) and / or a fluid in which at least one evaporator (4; 4a, 4b) has reached a predefined temperature or the temperature is above it.
    [14]
    14. Fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) for a motor vehicle (1000), comprising a fuel cell stack (1) with an anode section (2) and a cathode section (3), at least one Evaporator (4; 4a, 4b) for evaporating a fuel-water mixture, a reformer (5) for reforming the evaporated fuel-water mixture for use in the anode section (2) of the fuel cell stack (1), and at least one burner (6, 17) for burning a fuel-containing fluid, characterized in that the reformer (5) in particular downstream of the at least one evaporator (4; 4a, 4b) and the at least one burner (6, 17) in particular upstream of the at least one evaporator (4; 4a, 4b ) are arranged and the at least one burner (6, 17) with the at least one evaporator (4; 4a, 4b) for supplying fuel-containing fluid burned in the at least one burner (6, 17) from the at least e a burner (6, 17) to the
    27/47
    PP31603AT
    AVL List GmbH has at least one evaporator (4; 4a, 4b) in fluid communication and upstream of the at least one evaporator (4; 4a, 4b) a fuel-water mixture source (7; 7a, 7b) for providing a fuel-water mixture for the at least one evaporator (4; 4a, 4b) is arranged.
    [15]
    15. The fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to claim 14, characterized in that a control unit (19) is provided which is used to carry out a method according to one of claims 1 to 13 configured and configured.
    [16]
    16. The fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 15, characterized in that the fuel and the water in the fuel-water mixture source (7 ;
    7a; 7b) are provided at least temporarily in liquid form.
    [17]
    17. Fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 16, characterized in that the at least one evaporator (4; 4a, 4b) directly downstream of the fuel water Mixture source (7; 7a; 7b) is arranged.
    [18]
    18. Fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 17, characterized in that the at least one evaporator (4; 4a, 4b) directly downstream of the at least one Brenner (6, 17) is arranged.
    [19]
    19. Fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 18, characterized in that the at least one evaporator (4; 4a, 4b) and / or the reformer (5) are connected directly to the at least one burner (6, 17).
    [20]
    20. The fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 19,
    28/47
    PP31603AT
    AVL List GmbH, characterized in that the at least one burner has an exhaust burner (6) and / or a start burner (17).
    [21]
    21. Fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 20, characterized in that an air supply device (16), in particular a blower, for supplying air to the Reformer (5) is arranged before reforming or during the reforming of the evaporated fuel-water mixture.
    [22]
    22. Fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 21, characterized in that the at least one burner (6, 17) for burning anode exhaust gas from the anode section (2), of cathode exhaust gas from the cathode section (3) and / or of fuel from a fuel source (14) which is arranged upstream of the at least one burner (6, 17), the fuel source (14) for supplying the Fuel to the at least one burner (6, 17) is configured, and the at least one burner (6, 17) for supplying the burned fuel from the at least one burner (6, 17) to the at least one evaporator (4; 4a, 4b ), for heating the at least one evaporator (4; 4a, 4b) and / or the fluid within the at least one evaporator (4; 4a, 4b) to the target temperature or above.
    [23]
    23. The fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 22, characterized in that the at least one burner (6, 17) is an electrically activatable catalyst, in particular one Electrically heated metal catalyst for burning the fuel, wherein the catalyst is configured to be deactivated as soon as the target temperature is reached or exceeded.
    [24]
    24. The fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 23,
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    PP31603AT
    AVL List GmbH, characterized in that downstream of the fuel-water mixture source (7; 7a, 7b) and upstream of the at least one evaporator (4; 4a, 4b) at least one injector (12) for injecting the fuel-water mixture from the fuel-water mixture source (7; 7a, 7b) in the at least one evaporator (4; 4a, 4b) is arranged.
    [25]
    25. The fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 24, characterized in that on an outer wall section of the at least one burner (6, 17) a heat exchange section (18 ) is designed on or in which the fuel-water mixture evaporated by the at least one evaporator (4; 4a, 4b) can be fed to the at least one burner (6, 17).
    [26]
    26. Fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 25, characterized in that upstream of the at least one evaporator (4a) a fuel source (7a) for providing a Fuel for the at least one evaporator (4a) is arranged, fuel evaporated by the at least one evaporator (4a) for heating the fuel on or in a heat exchange section (18) of the at least one burner (6, 17) as the fuel-containing fluid to the at least one burner (6, 17) can be guided.
    [27]
    27. Fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 26, characterized in that downstream of the fuel-water mixture source (7; 7a, 7b) and / or the fuel source (7a) and upstream of the at least one burner (6, 17) an intermediate heating device (11), in particular an electrical intermediate heating device (11), is arranged for heating the fuel-water mixture or the fuel, the Intermediate heating device (11) is configured to heat the fuel-water mixture or the fuel until the fuel-water mixture or the fuel has reached a predefined temperature or the temperature is above it.
    30/47
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    [28]
    28. The fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to claim 27, characterized in that the intermediate heating device (11) is configured to be deactivated as soon as the at least one burner (6, 17th ), a fluid in the at least one burner which has at least one evaporator (4; 4a, 4b) and / or a fluid in the at least one evaporator (4; 4a, 4b) has reached a predefined temperature or the temperature is above it.
    [29]
    29. Motor vehicle (1000) with a fuel cell system (100a; 100b; 100c; 100d; 100e; 100f; 100g; 100h; 100i) according to one of claims 14 to 28.
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    同族专利:
    公开号 | 公开日
    WO2019068123A1|2019-04-11|
    AT520482B1|2019-11-15|
    BR112020006275A2|2020-10-06|
    CN111149245A|2020-05-12|
    US20200295388A1|2020-09-17|
    DE112018004566A5|2020-06-18|
    JP2020536358A|2020-12-10|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    AT508452017A|AT520482B1|2017-10-03|2017-10-03|Method for quickly heating up a fuel cell system|AT508452017A| AT520482B1|2017-10-03|2017-10-03|Method for quickly heating up a fuel cell system|
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