WO2022174276A1 - Wärmekopplungsvorrichtung für ein brennstoffzellensystem - Google Patents
Wärmekopplungsvorrichtung für ein brennstoffzellensystem Download PDFInfo
- Publication number
- WO2022174276A1 WO2022174276A1 PCT/AT2022/060045 AT2022060045W WO2022174276A1 WO 2022174276 A1 WO2022174276 A1 WO 2022174276A1 AT 2022060045 W AT2022060045 W AT 2022060045W WO 2022174276 A1 WO2022174276 A1 WO 2022174276A1
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- WO
- WIPO (PCT)
- Prior art keywords
- heat
- coupling
- exhaust gas
- fuel cell
- section
- Prior art date
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- 230000008878 coupling Effects 0.000 title claims abstract description 134
- 238000010168 coupling process Methods 0.000 title claims abstract description 134
- 238000005859 coupling reaction Methods 0.000 title claims abstract description 134
- 239000000446 fuel Substances 0.000 title claims abstract description 101
- 239000012530 fluid Substances 0.000 claims abstract description 66
- 238000004519 manufacturing process Methods 0.000 claims abstract description 61
- 238000012546 transfer Methods 0.000 claims abstract description 17
- 238000007599 discharging Methods 0.000 claims abstract 2
- 238000000034 method Methods 0.000 claims description 61
- 230000008569 process Effects 0.000 claims description 44
- 230000005611 electricity Effects 0.000 claims description 21
- 238000001816 cooling Methods 0.000 claims description 14
- 230000009467 reduction Effects 0.000 claims description 7
- 238000011144 upstream manufacturing Methods 0.000 claims description 5
- 238000004088 simulation Methods 0.000 claims description 4
- 238000005057 refrigeration Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 122
- 230000008901 benefit Effects 0.000 description 15
- 238000010438 heat treatment Methods 0.000 description 6
- 238000013461 design Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 239000013529 heat transfer fluid Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04007—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
- H01M8/04029—Heat exchange using liquids
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
- H01M8/04298—Processes for controlling fuel cells or fuel cell systems
- H01M8/04694—Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
- H01M8/04701—Temperature
- H01M8/04716—Temperature of fuel cell exhausts
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M8/00—Fuel cells; Manufacture thereof
- H01M8/10—Fuel cells with solid electrolytes
- H01M8/12—Fuel cells with solid electrolytes operating at high temperature, e.g. with stabilised ZrO2 electrolyte
- H01M2008/1293—Fuel cells with solid oxide electrolytes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2250/00—Fuel cells for particular applications; Specific features of fuel cell system
- H01M2250/10—Fuel cells in stationary systems, e.g. emergency power source in plant
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Definitions
- the present invention relates to a heat coupling device for a fuel cell system, a fuel cell system with such a heat coupling device and a method for coupling the use of electricity production and heat production of a fuel cell system.
- fuel cell systems are used to produce electricity in a stationary operating situation.
- a so-called SOFC fuel cell is used, which brings with it very high temperatures during operation.
- the operating temperature of a SOFC fuel cell in stationary operation is, for example, in the range of around 500 °C to 1000 °C.
- the hot exhaust gases which leave such a fuel cell system are partly used to preheat process gases, in particular the anode feed gas and/or the cathode feed gas. Nevertheless, a residual amount of heat remains in the exhaust gas of the fuel cell system, which is often given off to the environment.
- a disadvantage of the known solutions is that when electricity production and heat production are coupled, these two objectives are in conflict with one another.
- the control of the entire system is either current-controlled or heat-controlled. This means that either the heat demand is met and the electricity production is the result of the current heat demand, or vice versa.
- current-controlled regulation means that a specified amount of electricity is produced and the current heat production follows the electricity demand. Heat demand and electricity demand are therefore always coupled with one another and, in particular, cannot be controlled separately from one another. This leads to relatively complex control mechanisms and in particular to a very low control variability for heat use in a power-controlled control situation or power use in a heat-controlled control situation.
- a heat coupling device for a fuel cell system serves to couple the use of electricity production and heat production of the fuel cell system.
- the heat coupling device has an exhaust gas section for conducting hot exhaust gas from the fuel cell system.
- a coupling circuit for conducting a coupling fluid to a heat utilization device is also provided.
- the coupling circuit is equipped with a coupling heat exchanger, the hot side of which is arranged in the exhaust gas section, for transferring heat from the hot exhaust gas to the coupling fluid.
- an additional circuit is provided in the heat coupling device for Füh ren an additional fluid.
- the additional circuit has a delivery section for a delivery from heat from the additional fluid to the environment and a Additional heat exchanger, the hot side of which is arranged in the exhaust gas section, for the transfer of heat from the hot exhaust gas to the additional fluid.
- the core idea of the invention is based on making the heat that is present in the hot exhaust gas of the fuel cell system available to a heat utilization device.
- a heat utilization device can be a district heating network, for example, or a heating system for a building or an industrial plant.
- the heat is not or only partially released to the environment, but can be used in the heat utilization device.
- the coupling heat exchanger is arranged in the exhaust gas section.
- the coupling heat exchanger can be designed as a plate heat exchanger, for example.
- the hot side is formed directly or indirectly by the exhaust gas section, so that hot exhaust gas flows through the hot side of the coupling heat exchanger.
- the coupling fluid flows through the cold side, so that heat is transferred from the hot exhaust gas to the cold coupling fluid.
- the exhaust gas leaves the coupling heat exchanger cooler than it enters it.
- the coupling fluid is heated as it flows through the coupling heat exchanger and can in this way pass on the heat it has absorbed to the heat utilization device.
- the coupling fluid is designed in particular as a coupling liquid, example, in the form of water, thermal oil or the like.
- an additional circuit is now also planned.
- the additional circuit also circulates an additional fluid, which, similar to the coupling fluid, can be, for example, thermal oil, water or another fluid, in particular a liquid, which is capable of absorbing and transporting heat, in particular with a high specific heat capacity .
- the additional circuit is able to also absorb heat from the hot exhaust gas from the gas section, since the additional heat exchanger is also arranged with its hot side in the exhaust section. It is thus possible for hot exhaust gas not only to flow through the coupling heat exchanger on its hot side, but also through the hot side of the additional heat exchanger, at least in this way can also transfer part of the heat to the additional fluid.
- the additional circuit is preferably not or only in a small way equipped for using the heat taken up. Rather, the additional section serves to ensure that the total amount of heat absorbed by the additional fluid and the coupling fluid leads to a maximum residual temperature of the exhaust gas, which is not exceeded even with different amounts of heat to be used.
- the heat required ie the heat requirement
- the heat utilization device For example, the heat required, ie the heat requirement, varies at the heat utilization device. If the fuel cell system is in a current-controlled control situation, this varying heat requirement cannot be addressed. Rather, a resulting amount of heat is produced depending on the power requirement and the corresponding current-carrying control. Situations can now arise in which the current heat production significantly exceeds the current heat demand. Without the additional circuit, this would lead to a correspondingly lower amount of heat being extracted from the hot exhaust gas to meet the necessary heat requirement, as a result of which the hot exhaust gas would have an increased residual temperature when it flows out into the environment.
- the additional circuit can remain switched off and the heat can be essentially completely transferred from the hot exhaust gas to the coupling fluid.
- the heat production and the heat demand are now decoupled from one another.
- the fuel cell system can be operated with electricity and in the event that the heat requirement falls below the current heat production, the excess heat can be removed from the hot exhaust gas via the additional circuit. This leads to the desired decoupling and accordingly to the variable and flexible way of controlling the heat utilization device and the coupling circuit, even when the fuel cell system is controlled in a live manner.
- the additional cooling circuit can also have its own uses.
- the simplest possibility is that the exhaust gas is cooled via the additional circuit and the heat is given off to the environment.
- the advantages according to the invention of the described decoupling of electricity production and heat production come into play in particular in the case of fuel cell systems that are operated with negative pressure, in which a Vacuum conveying device is arranged downstream of the heat coupling device in the gas section from.
- the coupling circuit in particular does not necessarily have to have a closed circuit within the heat coupling device.
- cool coupling fluid is made available from a large heat coupling circuit and is heated in the manner described in the small coupling circuit of the heat coupling device.
- the flow and return are connected to one another in a fluid-communicating manner as a small circuit in the coupling circuit.
- the decoupling according to the invention makes it possible to ensure that the residual temperature does not exceed a defined limit temperature when the exhaust gas flows through the exhaust gas section.
- components and in particular a vacuum conveying device in the form of a suction fan can be protected from excessively high temperatures. This in turn leads to a simple and cost-effective configuration as well as a correspondingly simple and cost-effective choice of material for such a suction fan.
- the additional heat exchanger is arranged upstream of the coupling heat exchanger in the exhaust gas section. This allows a particularly flexible control and is based in particular on a detection of the current heat requirement in the heat utilization device and the current heat production in the fuel cell system.
- the hot exhaust gas is pre-cooled in the additional heat exchanger before the exhaust gas that has been pre-cooled in this way reaches the coupling heat exchanger.
- the additional circuit has an additional heat utilization device for using and/or storing the heat in the additional circuit.
- Storage can be provided by a heat storage device, for example. It is thus possible, in situations in which the heat production is below the heat requirement of the heat utilization device, to operate the additional circuit in the opposite direction, so to speak, and to discharge the heat accumulator again by transferring the stored heat from the heat accumulator in the opposite direction from the additional circuit to the exhaust gas is emitted.
- a delivery from the heat accumulator of the additional circuit directly to the coupling fluid, in particular special in the flow of the cold side of the coupling heat exchanger, is fundamentally conceivable.
- a separate heat utilization device such as an increase in efficiency in the fuel cell system and therefore independent of the coupling circuit, is of course also conceivable within the scope of this embodiment.
- a process heat exchanger is arranged in the exhaust gas section of a thermal coupling device according to the invention for transferring heat from the hot exhaust gas to at least one process gas fed to the fuel cell system.
- this process heat exchanger is arranged upstream of the coupling heat exchanger and/or upstream of the additional heat exchanger.
- the efficiency of the fuel cell system can be increased within the fuel cell system, in which process gases, for example the anode feed gas and/or the cathode feed gas, can be preheated.
- This process heat exchanger is preferably qualitatively and/or quantitatively controllable, so that this recirculation of heat can take place depending on the current operating situation of the fuel cell system and/or depending on the current heat requirement of the heat utilization device. Especially in a cold start situation when starting up the fuel cell system, possibilities for accelerating this starting process and increasing efficiency can be achieved here. It can also be advantageous if, in a thermal coupling device according to the invention, a process gas section is arranged separately from the exhaust gas section, for guiding a hot process gas of the fuel cell system, the coupling circuit having an intermediate heat exchanger downstream of the coupling heat exchanger, the hot side of which is arranged in the process gas section, for absorbing heat in the coupling fluid from the hot process gas.
- the process gas which is conducted in the process gas section, is preferably a process gas, which is led out of the fuel cell stack and fed back into it again.
- an intermediate cooling of the process gas is possible, which can be fed back to the fuel cell stack for further processing after the intermediate cooling. Additional heat transfer to the coupling fluid is also provided in this way.
- the coupling circuit has a bypass section for bypassing the coupling fluid past the intermediate heat exchanger.
- this intermediate cooling of the process gas can bring advantages, particularly temporarily, in individual operating situations.
- this intermediate heat exchanger can be switched on and off via the bypass, so to speak.
- a quantitative splitting of the coupling fluid between the by-pass section and the flow through the intermediate heat exchanger on its colder side is also possible. The variability, the possibility of control and/or the efficiency of the fuel cell system can be increased even further in this way.
- the additional circuit is designed as a refrigeration circuit. While in principle, either with passive funding or with forced funding, a normal cooling circuit is conceivable as an additional circuit, a cooling circuit with a compressor and an evaporator section in the additional heat exchanger can bring further advantages. In particular, this makes it possible to react even more freely to corresponding operating situations and temperature conditions in the hot exhaust gas by selecting a heat transfer medium as the additional fluid.
- the additional cooling circuit is designed for a maximum cooling capacity based on the maximum heat production of the fuel cell system. This means that even in the event that the heat requirement of the heat utilization device drops to zero, the entire heat production of a fuel cell system operated at maximum power can be dissipated via the additional circuit and in particular the additional heat exchanger. This means that even in the extreme situation of a switched off heat utilization device and accordingly a switched off heat transfer into the coupling fluid, the maximum temperature limit value for the residual temperature of the exhaust gas is not exceeded.
- the design is based on the amount of additional fluid, the corresponding flow cross-sections and other design options for the additional cooling circuit.
- the present invention also relates to a fuel cell system for generating electricity and heat.
- the fuel cell system includes a fuel cell stack having an anode section and a cathode section.
- the anode section is provided with an anode supply section and an anode discharge section.
- the cathode section is equipped with a cathode supply section and a cathode discharge section.
- the fuel cell system has a heat coupling device according to the present invention, whose exhaust gas section is connected to the anode discharge section and/or the cathode discharge section in a fluid-communicating manner.
- a fuel cell system according to the invention thus offers the same advantages as have been explained in detail with reference to a thermal coupling device according to the invention.
- a heat utilization device is preferably also integrated in this fuel cell system. It should also be noted that for the exhaust section Both a specific configuration for the anode discharge section or the cathode discharge section can be provided. However, it is also conceivable that, at least in part, the exhaust gas from the anode section in the anode discharge section and the exhaust gas from the cathode section in the cathode discharge section are combined to form a common exhaust gas and thus flow through the exhaust gas section of the heat coupling device as a common or combined exhaust gas.
- the fuel cell stack has a process gas section for guiding a process gas out of the fuel cell stack and back into the fuel cell stack, with an intermediate heat exchanger being arranged in the coupling circuit, the hot side of which is arranged in the process gas section , for absorbing heat in the coupling fluid of the process gas.
- a bypass section it is also possible for a bypass section to be provided in order to either qualitatively switch off this intermediate heat exchanger or to quantitatively control the amount of coupling fluid flowing through. As already explained, this allows intermediate cooling of the process gas as it flows through the fuel cell stack and thus a further increase in efficiency in the operation of the fuel cell system.
- Another object of the present invention is a method for coupling the use of electricity production and heat production of the fuel cell system according to the present invention. Such a procedure consists of the following steps:
- a method according to the invention brings with it the same advantages as have been explained in detail with reference to a heat coupling device according to the invention and with reference to a fuel cell system according to the invention. It should be noted that here the electricity production is used for the control of the fuel cell system. In other words, the control of the fuel cell system is current-controlled and not heat-controlled.
- the result is a resulting heat production, which is recorded as part of a method according to the invention and compared with a likewise recorded current heat requirement of the heat utilization device.
- a resulting heat production which is recorded as part of a method according to the invention and compared with a likewise recorded current heat requirement of the heat utilization device.
- the additional circuit can essentially be switched off or remain so. Rather, there is complete or essentially complete heat transfer from the hot exhaust gas to the coupling fluid, so that the heat requirement of the heat utilization device is met and at the same time the exhaust gas can be cooled below the maximum temperature limit value.
- the third operating situation to be distinguished from this occurs when the current heat production exceeds the current heat demand of the heat utilization device.
- the heat drawn off in the coupling fluid will not be sufficient to sufficiently cool the temperature of the exhaust gas while complying with the maximum temperature limit value.
- the cooling that is still missing is provided by the additional heat exchanger and the additional circuit.
- the heat transfer at the additional heat exchanger is more or less intense. This leads to the decoupling explained several times, so that despite a current-controlled control of the fuel cell system, a variation of the heat requirement of the heat utilization device is possible.
- the heat reduction via the additional heat exchanger is controlled by varying at least one of the following parameters:
- the mass flow of additional fluid in the additional circuit can be increased in order to correspondingly increase the heat transfer at the additional heat exchanger.
- the release of heat in the release section can be increased, so that the return temperature in the additional circuit for the additional fluid is reduced. This also serves to increase the heat transfer at the additional heat exchanger by increasing the temperature gradient accordingly.
- a temperature reduction for the exhaust gas in the exhaust gas section and/or an outlet temperature of the exhaust gas is determined from the detected heat requirement and the detected heat production. In both cases, it is preferably a simulation of the recorded heat requirement and/or a simulation of the current heat production. This makes it possible to foresee what temperature reduction and/or outlet temperature will occur for the exhaust gas and to carry out the control with a method according to the invention in a correspondingly more targeted manner.
- the recorded heat production and/or the recorded heat requirement is determined in advance by means of a simulation. In other words, it is possible to predict how the heat demand and/or heat production will develop over a defined period of time. This allows to avoid hunting or undesired increase over an interval for the temperature of the exhaust gas ensure that the limit values described are complied with over the maximum period of time during operation of the fuel cell system.
- FIG. 2 another embodiment of a heat coupling device according to the invention
- Fig. 6 an embodiment of a fuel cell system according to the invention
- Fig. 7 shows a possible course of the amounts of heat in a method according to the invention.
- FIG. 1 schematically shows a fuel cell system 100 in which one or more process gases P are fed to a fuel cell stack 110 .
- An exhaust gas A can be conducted out of the fuel cell stack 110 either as a collective exhaust gas or as an individual exhaust gas in the form of an exhaust gas section 20 of the thermal coupling device 10 .
- the hot exhaust gas A now flows through an additional heat exchanger 42 when guided in the exhaust gas section 20. In this heat is transferred from the hot exhaust gas A to the additional fluid ZF, which is promoted by a conveyor device 48 in the circuit of the additional circuit.
- the additional fluid ZF is now delivered in heated form along the additional circuit 40 to the delivery section 44 supplied.
- a fan device controls how much heat is given off to the environment by the additional fluid ZF.
- the mass flow of additional fluid ZF can be varied by controlling the delivery device 48 .
- the exhaust gas A pre-cooled in this way flows further along the exhaust gas section 20 into a coupling heat exchanger 32.
- the exhaust gas A which is now maximally cooled in this way, can be discharged to the environment.
- the heated coupling fluid KF can pass this heat on to the heat utilization device 200.
- the current heat requirement WB of the heat utilization device 200 can be lower, higher or identical to the current heat production WP of the fuel cell system 100 .
- auxiliary circuit 40 may be substantially off. This is ensured in particular by stopping the conveying device 48 .
- the excess heat can be transferred to the additional fluid ZF by increasing the speed of the conveyor device 48 with a correspondingly increased heat transfer at the additional heat exchanger 42, so that this too If the residual temperature in the exhaust gas A remains identical or essentially identically low when it exits into the environment.
- FIG. 2 shows a further development of the embodiment of FIG. 1.
- This relates to the conveyance of the process gases P through the fuel cell system 100.
- the suction fan 50 With the aid of the suction fan 50, a negative pressure is generated, which conveys the process gases P through the fuel cell system 100 and the exhaust gas A from the fuel cell stack 110.
- this suction fan 50 is not required to have resistance to high temperatures. It is therefore effectively protected against elevated temperatures in the exhaust gas A by the interaction of the coupling circuit 30 and the additional circuit 40 .
- FIG. 3 has an additional heat utilization device 46 as part of the additional circuit 40 .
- This can be a heat accumulator, for example, whose heat can be used for another purpose or, not shown here, by a heat transfer option to the coupling fluid KF upstream of the coupling heat exchanger 32, this heat can continue to be used efficiently.
- FIG. 4 shows a possibility of preheating process gases P, in particular in a starting situation of the fuel cell system 100.
- process gas P can be preheated with part of the heat contained in the exhaust gas A before it enters the fuel cell stack 110, so that the efficiency in this operating situation for the operation of the fuel cell system 100 increases further.
- FIG. 5 also shows a constructive possibility of further increasing the efficiency during operation of the fuel cell system 100.
- a recirculation is provided within the fuel cell system 100, which decouples a process gas P from the fuel cell stack 110, conducts it via an intermediate heat exchanger 34 and conveys it back into the fuel cell stack 110.
- the coupling fluid KF downstream of the coupling heat exchanger 32 either also flows through the intermediate heat exchanger 34 or through the bypass section 36 past it.
- this makes it possible to provide a further increase in the heat content of the coupling fluid KF.
- the efficiency of the mode of operation of the fuel cell system 100 can be increased in that an integrated possibility of reducing the temperature of process gases P within the fuel cell stack 110 is made available.
- FIG. 6 shows an embodiment similar to that in FIGS. 1 to 5. However, more details in the fuel cell stack 110 can be seen here.
- This one is in one Anode section 120 and divided into a cathode section 130 .
- An anode feed gas runs as process gases P in the anode feed section 122 and a cathode feed gas in the cathode feed section 132.
- Cathode off-gas is discharged in the cathode discharge section 134 .
- all of the exhaust gases A of the fuel cell stack are brought together and conveyed together as a common exhaust gas A through the exhaust gas section 20 in the manner already explained.
- FIG. 7 shows how a method according to the invention works.
- Heat demand WB and heat production WP are shown here over time.
- the heat requirement WB of the heat utilization device 200 is above the heat production WP of the fuel cell system 100.
- the heat requirement WB reduces over time until it falls below the current heat production WP at the arrow.
- the additional cooling is now switched on and/or increased with the aid of the additional circuit 30 .
- the heat requirement WB and the heat production WP can be the currently recorded parameters and/or simulated future parameter values.
- thermal coupling device 20 exhaust gas section 22 process heat exchanger 30 coupling circuit 32 coupling heat exchanger 34 intermediate heat exchanger 36 bypass section 40 additional circuit 42 additional heat exchanger 44 discharge section 46 additional heat utilization device 48 conveying device 50 suction fan
- fuel cell system 110 fuel cell stack 120 anode section 122 anode supply section 124 anode discharge section 130 cathode section 132 cathode supply section 134 cathode discharge section 140 process gas section 200 heat utilization device
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Abstract
Description
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Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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DE112022000377.4T DE112022000377A5 (de) | 2021-02-18 | 2022-02-18 | Wärmekopplungsvorrichtung für ein Brennstoffzellensystem |
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Application Number | Priority Date | Filing Date | Title |
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ATA50107/2021 | 2021-02-18 | ||
ATA50107/2021A AT524819B1 (de) | 2021-02-18 | 2021-02-18 | Wärmekopplungsvorrichtung für ein Brennstoffzellensystem |
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WO2022174276A1 true WO2022174276A1 (de) | 2022-08-25 |
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PCT/AT2022/060045 WO2022174276A1 (de) | 2021-02-18 | 2022-02-18 | Wärmekopplungsvorrichtung für ein brennstoffzellensystem |
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AT (1) | AT524819B1 (de) |
DE (1) | DE112022000377A5 (de) |
WO (1) | WO2022174276A1 (de) |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102009034580A1 (de) * | 2009-07-24 | 2011-02-03 | Mtu Onsite Energy Gmbh | Einrichtung zur Bereitstellung von Energie |
EP2884572A1 (de) * | 2012-08-07 | 2015-06-17 | Kyocera Corporation | Hybridsystem |
EP3051228A1 (de) * | 2013-09-27 | 2016-08-03 | Kyocera Corporation | Kühl- und heizvorrichtung |
JP2019168180A (ja) * | 2018-03-23 | 2019-10-03 | 三浦工業株式会社 | 冷温水機複合型燃料電池システム |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
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DE10031864C1 (de) * | 2000-06-30 | 2002-06-20 | Zsw | Verfahren zur Regelung des wärme- und/oder strombedarfsgeführten Betriebs von Brennstoffzellenanlagen |
CN111446467B (zh) * | 2020-03-27 | 2023-09-15 | 上海电气集团股份有限公司 | 燃料电池热电联供系统及其控制方法 |
-
2021
- 2021-02-18 AT ATA50107/2021A patent/AT524819B1/de active
-
2022
- 2022-02-18 WO PCT/AT2022/060045 patent/WO2022174276A1/de active Application Filing
- 2022-02-18 DE DE112022000377.4T patent/DE112022000377A5/de active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102009034580A1 (de) * | 2009-07-24 | 2011-02-03 | Mtu Onsite Energy Gmbh | Einrichtung zur Bereitstellung von Energie |
EP2884572A1 (de) * | 2012-08-07 | 2015-06-17 | Kyocera Corporation | Hybridsystem |
EP3051228A1 (de) * | 2013-09-27 | 2016-08-03 | Kyocera Corporation | Kühl- und heizvorrichtung |
JP2019168180A (ja) * | 2018-03-23 | 2019-10-03 | 三浦工業株式会社 | 冷温水機複合型燃料電池システム |
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Publication number | Publication date |
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AT524819A1 (de) | 2022-09-15 |
AT524819B1 (de) | 2023-11-15 |
DE112022000377A5 (de) | 2023-09-21 |
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