CN110957504B - Fuel cell power system - Google Patents

Fuel cell power system Download PDF

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CN110957504B
CN110957504B CN201911153362.3A CN201911153362A CN110957504B CN 110957504 B CN110957504 B CN 110957504B CN 201911153362 A CN201911153362 A CN 201911153362A CN 110957504 B CN110957504 B CN 110957504B
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outlet
heat exchanger
fuel cell
power system
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胡尊严
李建秋
徐梁飞
欧阳明高
宋金鹏
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Tsinghua University
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04029Heat exchange using liquids
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04201Reactant storage and supply, e.g. means for feeding, pipes
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/04Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04298Processes for controlling fuel cells or fuel cell systems
    • H01M8/04694Processes for controlling fuel cells or fuel cell systems characterised by variables to be controlled
    • H01M8/04701Temperature
    • H01M8/04738Temperature of auxiliary devices, e.g. reformer, compressor, burner
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/22Fuel cells in which the fuel is based on materials comprising carbon or oxygen or hydrogen and other elements; Fuel cells in which the fuel is based on materials comprising only elements other than carbon, oxygen or hydrogen
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/24Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465Details of groupings of fuel cells
    • H01M8/2483Details of groupings of fuel cells characterised by internal manifolds
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2250/00Fuel cells for particular applications; Specific features of fuel cell system
    • H01M2250/20Fuel cells in motive systems, e.g. vehicle, ship, plane
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

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Abstract

本申请涉及一种燃料电池动力系统。所述燃料电池动力系统包括电池堆、电堆换热器、电机和液氢罐。所述燃料电池动力系统将液态氢直接作为热交换介质进入所述冷却壳,所述液态氢的温度升高,同时所述电机的温度降低至‑150℃以下,让电机工作在超导状态。所述液态氢在作为换热介质进入所述电堆换热器吸收热量。所述燃料电池动力系统使得液态氢的气化效率更高,同时降低了电机的发热损耗。进一步的,所述燃料电池动力系统将液态氢直接作为热交换介质参与换热,无需额外设置换热器,实现轻量化设计。同时,所述系统采用单层液氢存储结构,进一步降低了系统重量。

Figure 201911153362

The present application relates to a fuel cell power system. The fuel cell power system includes a battery stack, a stack heat exchanger, a motor and a liquid hydrogen tank. The fuel cell power system directly enters the cooling shell with liquid hydrogen as a heat exchange medium, the temperature of the liquid hydrogen increases, and at the same time the temperature of the motor is lowered to below -150°C, allowing the motor to work in a superconducting state. The liquid hydrogen enters the stack heat exchanger as a heat exchange medium to absorb heat. The fuel cell power system makes the gasification efficiency of liquid hydrogen higher, and at the same time reduces the heat loss of the motor. Further, the fuel cell power system uses liquid hydrogen directly as a heat exchange medium to participate in heat exchange, and no additional heat exchanger is required to achieve a lightweight design. At the same time, the system adopts a single-layer liquid hydrogen storage structure, which further reduces the weight of the system.

Figure 201911153362

Description

燃料电池动力系统fuel cell power system

技术领域technical field

本申请涉及电池技术领域,特别是涉及一种燃料电池动力系统。The present application relates to the field of battery technology, in particular to a fuel cell power system.

背景技术Background technique

燃料电池动力系统开始逐步替换传统的内燃机动力系统,应用于汽车、舰船、航空等交通运输设备。氢气是燃料电池系统的反应燃料,氢气携带量的多少决定了系统所能发出的总电能。尤其将燃料电池用于无人机、飞机等系统时,系统能量密度与功率密度对于无人机、飞机等系统总体性能十分关键。现有技术中,液氢汽化、燃料电池冷却、电机冷却、电机发热所消耗的能量大幅降低了系统效率,限制了续航里程的提高。The fuel cell power system has begun to gradually replace the traditional internal combustion engine power system, and is used in transportation equipment such as automobiles, ships, and aviation. Hydrogen is the reaction fuel of the fuel cell system, and the amount of hydrogen carried determines the total electricity that the system can generate. Especially when fuel cells are used in UAVs, aircraft and other systems, the system energy density and power density are very critical to the overall performance of UAVs, aircraft and other systems. In the prior art, the energy consumed by the vaporization of liquid hydrogen, the cooling of the fuel cell, the cooling of the motor, and the heating of the motor greatly reduces the system efficiency and limits the improvement of the cruising range.

发明内容SUMMARY OF THE INVENTION

基于此,有必要针对怎样提高燃料电池动力系统能量利用效率的问题,提供一种燃料电池动力系统。Based on this, it is necessary to provide a fuel cell power system for the problem of how to improve the energy utilization efficiency of the fuel cell power system.

一种燃料电池动力系统,包括电池堆、电堆换热器、电机和液氢罐。所述电池堆包括氢气入口、热水出口、冷水进口、电力输出口。所述电堆换热器包括冷却液进口、冷却液出口、待冷液进口和待冷液出口。所述待冷液进口与所述热水出口连通。所述待冷液出口与所述冷水进口连通。所述电力输出口与所述电机电连接。所述电机包括冷却壳。所述冷却壳包括第一进口和第一出口。所述液氢罐包括液氢出口。所述液氢出口与所述第一进口连通。所述第一出口与所述冷却液进口连通。所述冷却液出口与所述氢气入口连通。A fuel cell power system includes a battery stack, a stack heat exchanger, a motor and a liquid hydrogen tank. The battery stack includes a hydrogen inlet, a hot water outlet, a cold water inlet, and an electric power outlet. The stack heat exchanger includes a cooling liquid inlet, a cooling liquid outlet, an inlet for cooling liquid and an outlet for cooling liquid. The inlet of the liquid to be cooled is communicated with the outlet of the hot water. The to-be-cooled liquid outlet communicates with the cold water inlet. The power outlet is electrically connected to the motor. The electric machine includes a cooling shell. The cooling shell includes a first inlet and a first outlet. The liquid hydrogen tank includes a liquid hydrogen outlet. The liquid hydrogen outlet communicates with the first inlet. The first outlet communicates with the coolant inlet. The cooling liquid outlet communicates with the hydrogen inlet.

在一个实施例中,所述燃料电池动力系统还包括第一储液装置和第一电子泵。所述第一储液装置连接于所述待冷液出口与所述冷水进口之间。所述第一电子泵连接于所述第一储液装置与所述冷水进口之间。In one embodiment, the fuel cell power system further includes a first liquid storage device and a first electronic pump. The first liquid storage device is connected between the to-be-cooled liquid outlet and the cold water inlet. The first electronic pump is connected between the first liquid storage device and the cold water inlet.

在一个实施例中,所述燃料电池动力系统还包括第一减压阀。所述第一减压阀设置于所述冷却液出口与所述氢气入口之间。In one embodiment, the fuel cell power system further includes a first relief valve. The first pressure reducing valve is arranged between the cooling liquid outlet and the hydrogen inlet.

在一个实施例中,所述液氢罐为单层壳体结构。In one embodiment, the liquid hydrogen tank has a single-layer shell structure.

在一个实施例中,所述电机为超导电机,通过液氢冷却达到超导工作状态。In one embodiment, the motor is a superconducting motor, which is cooled by liquid hydrogen to achieve a superconducting working state.

本申请实施例提供所述燃料电池动力系统包括电池堆、电堆换热器、电机和液氢罐。所述电池堆包括氢气入口、热水出口、冷水进口、电力输出口。所述电堆换热器包括冷却液进口、冷却液出口、待冷液进口和待冷液出口。所述待冷液进口与所述热水出口连通。所述待冷液出口与所述冷水进口连通。所述电力输出口与所述电机电连接。所述电机包括冷却壳。所述冷却壳包括第一进口和第一出口。所述液氢罐包括液氢出口。所述液氢出口与所述第一进口连通。所述第一出口与所述冷却液进口连通。所述冷却液出口与所述氢气入口连通。The embodiments of the present application provide that the fuel cell power system includes a battery stack, a stack heat exchanger, a motor, and a liquid hydrogen tank. The battery stack includes a hydrogen inlet, a hot water outlet, a cold water inlet, and an electric power outlet. The stack heat exchanger includes a cooling liquid inlet, a cooling liquid outlet, an inlet for cooling liquid and an outlet for cooling liquid. The inlet of the liquid to be cooled is communicated with the outlet of the hot water. The to-be-cooled liquid outlet communicates with the cold water inlet. The power outlet is electrically connected to the motor. The electric machine includes a cooling shell. The cooling shell includes a first inlet and a first outlet. The liquid hydrogen tank includes a liquid hydrogen outlet. The liquid hydrogen outlet communicates with the first inlet. The first outlet communicates with the coolant inlet. The cooling liquid outlet communicates with the hydrogen inlet.

所述燃料电池动力系统使液态氢直接作为热交换介质进入所述冷却壳,吸收所述电机的热量,使得电机工作温度降低到-150℃以下,使得电机进入超导状态,避免了电机绕组发热损耗能量。所述液态氢在作为换热介质进入所述电堆换热器进一步吸收热量。所述燃料电池动力系统避免了电机发热损耗与电机散热损耗,并将液氢气化耗能用于燃料电池冷却,大幅提高系统效率。进一步的,所述燃料电池动力系统使用液态氢直接作为热交换介质参与换热,无需额外设置换热器,实现轻量化设计。The fuel cell power system makes liquid hydrogen directly enter the cooling shell as a heat exchange medium, absorbs the heat of the motor, reduces the working temperature of the motor to below -150°C, makes the motor enter a superconducting state, and avoids the heating of the motor windings loss of energy. The liquid hydrogen enters the stack heat exchanger as a heat exchange medium to further absorb heat. The fuel cell power system avoids the heat loss of the motor and the heat dissipation loss of the motor, and uses the liquid hydrogen gasification energy to cool the fuel cell, thereby greatly improving the system efficiency. Further, the fuel cell power system uses liquid hydrogen directly as a heat exchange medium to participate in heat exchange without additional heat exchangers, thereby realizing a lightweight design.

一种燃料电池动力系统包括电池堆、电堆换热器、电机、液氢罐、缓冲罐和换热装置。所述电池堆包括氢气入口、热水出口、冷水进口、电力输出口。所述电堆换热器包括待冷液进口和待冷液出口。所述待冷液进口与所述热水出口连通。所述待冷液出口与所述冷水进口连通。所述电机与所述电力输出口电连接。所述液氢罐用于存储液态氢气。所述液氢罐包括液氢出口。所述缓冲罐包括进液口和出液口。所述进液口与所述液氢出口连通。所述出液口与所述氢气入口连通。A fuel cell power system includes a battery stack, a stack heat exchanger, a motor, a liquid hydrogen tank, a buffer tank and a heat exchange device. The battery stack includes a hydrogen inlet, a hot water outlet, a cold water inlet, and an electric power outlet. The stack heat exchanger includes an inlet for liquid to be cooled and an outlet for liquid to be cooled. The inlet of the liquid to be cooled is communicated with the outlet of the hot water. The to-be-cooled liquid outlet communicates with the cold water inlet. The motor is electrically connected to the power outlet. The liquid hydrogen tank is used for storing liquid hydrogen. The liquid hydrogen tank includes a liquid hydrogen outlet. The buffer tank includes a liquid inlet and a liquid outlet. The liquid inlet is communicated with the liquid hydrogen outlet. The liquid outlet communicates with the hydrogen inlet.

所述换热装置包括闭环连通的第二储液装置、第一换热器、第二换热器和第三换热器。所述第二储液装置用于储存热交换介质。所述第一换热器用于与所述缓冲罐热交换。所述第二换热器用于与所述电堆换热器热交换。所述第三换热器用于与所述电机热交换。The heat exchange device includes a closed-loop communication second liquid storage device, a first heat exchanger, a second heat exchanger and a third heat exchanger. The second liquid storage device is used for storing heat exchange medium. The first heat exchanger is used for heat exchange with the buffer tank. The second heat exchanger is used for heat exchange with the stack heat exchanger. The third heat exchanger is used for heat exchange with the motor.

在一个实施例中,所述燃料电池动力系统还包括第二储液装置和第一电子泵。所述第二储液装置连接于所述待冷液出口与所述冷水进口之间。所述第一电子泵连接于所述第二储液装置与所述冷水进口之间。In one embodiment, the fuel cell power system further includes a second liquid storage device and a first electronic pump. The second liquid storage device is connected between the to-be-cooled liquid outlet and the cold water inlet. The first electronic pump is connected between the second liquid storage device and the cold water inlet.

在一个实施例中,所述燃料电池动力系统还包括第二电子泵。所述第二电子泵连接于所述第二储液装置与所述第一换热器之间。In one embodiment, the fuel cell power system further includes a second electronic pump. The second electronic pump is connected between the second liquid storage device and the first heat exchanger.

在一个实施例中,所述第二电子泵的出口与所述第一换热器的入口连通。In one embodiment, the outlet of the second electronic pump communicates with the inlet of the first heat exchanger.

在一个实施例中,所述换热装置还包括第四换热器。所述第四换热器连接于所述第二换热器与所述第三换热器之间。所述燃料电池动力系统还包括电机控制器。所述电机控制器与所述电机的信号输入端电连接。所述第四换热器用于与所述电极控制器交换热量。In one embodiment, the heat exchange device further includes a fourth heat exchanger. The fourth heat exchanger is connected between the second heat exchanger and the third heat exchanger. The fuel cell power system also includes a motor controller. The motor controller is electrically connected to the signal input end of the motor. The fourth heat exchanger is used for exchanging heat with the electrode controller.

本申请实施例提供的燃料电池动力系统包括电池堆、电堆换热器、电机、液氢罐、缓冲罐和换热装置。所述电池堆包括氢气入口、热水出口、冷水进口、电力输出口。所述电堆换热器包括待冷液进口和待冷液出口。所述待冷液进口与所述热水出口连通。所述待冷液出口与所述冷水进口连通。所述电机与所述电力输出口电连接。所述液氢罐用于存储液态氢气。所述液氢罐包括液氢出口。所述缓冲罐包括进液口和出液口。所述进液口与所述液氢出口连通。所述出液口与所述氢气入口连通。所述换热装置包括闭环连通的第二储液装置、第一换热器、第二换热器和第三换热器。所述第二储液装置用于储存热交换介质。所述第一换热器用于与所述缓冲罐热交换。所述第二换热器用于与所述电堆换热器热交换。所述第三换热器用于与所述电机热交换。The fuel cell power system provided by the embodiments of the present application includes a battery stack, a stack heat exchanger, a motor, a liquid hydrogen tank, a buffer tank, and a heat exchange device. The battery stack includes a hydrogen inlet, a hot water outlet, a cold water inlet, and an electric power outlet. The stack heat exchanger includes an inlet for liquid to be cooled and an outlet for liquid to be cooled. The inlet of the liquid to be cooled is communicated with the outlet of the hot water. The to-be-cooled liquid outlet communicates with the cold water inlet. The motor is electrically connected to the power outlet. The liquid hydrogen tank is used for storing liquid hydrogen. The liquid hydrogen tank includes a liquid hydrogen outlet. The buffer tank includes a liquid inlet and a liquid outlet. The liquid inlet is communicated with the liquid hydrogen outlet. The liquid outlet communicates with the hydrogen inlet. The heat exchange device includes a closed-loop communication second liquid storage device, a first heat exchanger, a second heat exchanger and a third heat exchanger. The second liquid storage device is used for storing heat exchange medium. The first heat exchanger is used for heat exchange with the buffer tank. The second heat exchanger is used for heat exchange with the stack heat exchanger. The third heat exchanger is used for heat exchange with the motor.

所述燃料电池动力系统通过所述第一换热器吸收液氢的冷量,热交换介质降温,同时液态氢气转变为气态氢气。所述气态氢气供所述电池堆反应生成电能。所述电池堆的电能为所述电机供电。所述电池堆在反应过程中产生热量。所述热量由循环水带入所述电堆换热器。低温的热交换介质先通过所述第二换热器为循环水降温,再通过所述第三换热器为所述电机降温,使所述电机高效工作。所述燃料电池动力系统通过所述换热装置实现内部冷量和热量互补,提高了所述燃料电池动力系统内部能量利用效率。进一步的,所述燃料电池动力系统减少了外部冷源和热源设置,实现轻量化设计。所述燃料电池动力系统使用间接冷却介质,与液态氢进行热交换加热,介质分别串联液氢、电机、电机控制器与燃料电池,将各个部件发热的能量用于液氢气化,有效降低了系统散热与加热的能耗,使得系统效率更高。The fuel cell power system absorbs the cold energy of the liquid hydrogen through the first heat exchanger, the heat exchange medium cools down, and the liquid hydrogen is converted into gaseous hydrogen at the same time. The gaseous hydrogen is used for the stack to react to generate electrical energy. The electrical energy of the battery stack powers the electric motor. The stack generates heat during the reaction. The heat is brought into the stack heat exchanger by circulating water. The low-temperature heat exchange medium first cools the circulating water through the second heat exchanger, and then cools the motor through the third heat exchanger, so that the motor works efficiently. The fuel cell power system realizes the complementation of internal cooling capacity and heat through the heat exchange device, thereby improving the internal energy utilization efficiency of the fuel cell power system. Further, the fuel cell power system reduces the arrangement of external cooling sources and heat sources, and realizes a lightweight design. The fuel cell power system uses an indirect cooling medium for heat exchange and heating with liquid hydrogen. The medium is connected in series with liquid hydrogen, a motor, a motor controller and a fuel cell respectively, and the energy generated by each component is used for liquid hydrogen gasification, which effectively reduces the system. The energy consumption of heat dissipation and heating makes the system more efficient.

附图说明Description of drawings

图1为本申请一个实施例中提供的所述燃料电池动力系统的电气原理图;FIG. 1 is an electrical schematic diagram of the fuel cell power system provided in an embodiment of the application;

图2为本申请另一个实施例中提供的所述燃料电池动力系统的电气原理图。FIG. 2 is an electrical schematic diagram of the fuel cell power system provided in another embodiment of the present application.

附图标号:Reference number:

燃料电池动力系统10Fuel Cell Power System 10

电池堆20battery stack 20

氢气入口201Hydrogen inlet 201

热水出口202Hot water outlet 202

冷水进口203Cold water inlet 203

电力输出口204Power outlet 204

电堆换热器30Stack Heat Exchanger 30

待冷液进口301Waiting for coolant inlet 301

待冷液出口302Waiting for coolant outlet 302

冷却液进口303Coolant inlet 303

冷却液出口304Coolant outlet 304

第一储液装置310The first liquid storage device 310

第一电子泵320first electronic pump 320

电机40Motor 40

信号输入端400Signal input 400

冷却壳401Cooling Shell 401

第一进口402First Import 402

第一出口403First exit 403

电机控制器410Motor Controller 410

液氢罐50Liquid hydrogen tank 50

液氢出口501Liquid hydrogen outlet 501

缓冲罐60Buffer Tank 60

进液口601Liquid inlet 601

出液口602Liquid outlet 602

换热装置70Heat Exchanger 70

第二储液装置710Second liquid storage device 710

第一换热器720first heat exchanger 720

第二换热器730Second heat exchanger 730

第三换热器740Third heat exchanger 740

第二电子泵750Second electronic pump 750

第四换热器760Fourth heat exchanger 760

第一减压阀80first pressure relief valve 80

具体实施方式Detailed ways

为使本申请的上述目的、特征和优点能够更加明显易懂,下面结合附图对本申请的具体实施方式做详细的说明。在下面的描述中阐述了很多具体细节以便于充分理解本申请。但是本申请能够以很多不同于在此描述的其它方式来实施,本领域技术人员可以在不违背本申请内涵的情况下做类似改进,因此本申请不受下面公开的具体实施的限制。In order to make the above objects, features and advantages of the present application more clearly understood, the specific embodiments of the present application will be described in detail below with reference to the accompanying drawings. In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present application. However, the present application can be implemented in many other ways different from those described herein, and those skilled in the art can make similar improvements without departing from the connotation of the present application. Therefore, the present application is not limited by the specific implementation disclosed below.

本文中为部件所编序号本身,例如“第一”、“第二”等,仅用于区分所描述的对象,不具有任何顺序或技术含义。而本申请所说“连接”、“联接”,如无特别说明,均包括直接和间接连接(联接)。在本申请的描述中,需要理解的是,术语“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”、“内”、“外”、“顺时针”、“逆时针”等指示的方位或位置关系为基于附图所示的方位或位置关系,仅是为了便于描述本申请和简化描述,而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作,因此不能理解为对本申请的限制。The serial numbers themselves, such as "first", "second", etc., for the components herein are only used to distinguish the described objects, and do not have any order or technical meaning. The "connection" and "connection" mentioned in this application, unless otherwise specified, include both direct and indirect connections (connections). In the description of this application, it should be understood that the terms "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", The orientation or positional relationship indicated by "bottom", "inner", "outer", "clockwise", "counterclockwise", etc. is based on the orientation or positional relationship shown in the drawings, and is only for the convenience of describing the present application and simplifying the description , rather than indicating or implying that the referred device or element must have a particular orientation, be constructed and operate in a particular orientation, and therefore should not be construed as a limitation on the present application.

在本申请中,除非另有明确的规定和限定,第一特征在第二特征“上”或“下”可以是第一和第二特征直接接触,或第一和第二特征通过中间媒介间接接触。而且,第一特征在第二特征“之上”、“上方”和“上面”可是第一特征在第二特征正上方或斜上方,或仅仅表示第一特征水平高度高于第二特征。第一特征在第二特征“之下”、“下方”和“下面”可以是第一特征在第二特征正下方或斜下方,或仅仅表示第一特征水平高度小于第二特征。In this application, unless otherwise expressly stated and defined, a first feature "on" or "under" a second feature may be in direct contact with the first and second features, or the first and second features indirectly through an intermediary touch. Also, the first feature being "above", "over" and "above" the second feature may mean that the first feature is directly above or obliquely above the second feature, or simply means that the first feature is level higher than the second feature. The first feature being "below", "below" and "below" the second feature may mean that the first feature is directly below or obliquely below the second feature, or simply means that the first feature has a lower level than the second feature.

请参见图1,本申请实施例提供一种燃料电池动力系统10包括电池堆20、电堆换热器30、电机40和液氢罐50。所述电池堆20包括氢气入口201、热水出口202、冷水进口203、电力输出口204。所述电堆换热器30包括冷却液进口303、冷却液出口304、待冷液进口301和待冷液出口302。所述待冷液进口301与所述热水出口202连通。所述待冷液出口302与所述冷水进口203连通。所述电力输出口204与所述电机40电连接。所述电机40包括冷却壳401。所述冷却壳401包括第一进口402和第一出口403。所述液氢罐50包括液氢出口501。所述液氢出口501与所述第一进口402连通。所述第一出口403与所述冷却液进口303连通。所述冷却液出口304与所述氢气入口201连通。Referring to FIG. 1 , an embodiment of the present application provides a fuel cell power system 10 including a battery stack 20 , a stack heat exchanger 30 , a motor 40 and a liquid hydrogen tank 50 . The battery stack 20 includes a hydrogen inlet 201 , a hot water outlet 202 , a cold water inlet 203 , and a power outlet 204 . The stack heat exchanger 30 includes a cooling liquid inlet 303 , a cooling liquid outlet 304 , an inlet 301 for cooling liquid and an outlet 302 for cooling liquid. The to-be-cooled liquid inlet 301 communicates with the hot water outlet 202 . The to-be-cooled liquid outlet 302 communicates with the cold water inlet 203 . The power outlet 204 is electrically connected to the motor 40 . The motor 40 includes a cooling shell 401 . The cooling shell 401 includes a first inlet 402 and a first outlet 403 . The liquid hydrogen tank 50 includes a liquid hydrogen outlet 501 . The liquid hydrogen outlet 501 communicates with the first inlet 402 . The first outlet 403 communicates with the cooling liquid inlet 303 . The cooling liquid outlet 304 communicates with the hydrogen inlet 201 .

本申请实施例提供的所述燃料电池动力系统10将液态氢直接作为热交换介质进入所述冷却壳401,吸收所述电机40的热量,所述液态氢的温度升高,同时所述电机40的温度降低,使得电机温度逐步降低到-150℃以下,进入超导状态。所述液态氢在作为换热介质进入所述电堆换热器30吸收热量。所述燃料电池动力系统10使得所述液态氢两次吸热。所述液态氢的气化效率更高。进一步的,所述燃料电池动力系统10使液态氢直接作为热交换介质参与换热,无需额外设置换热器,实现轻量化设计。The fuel cell power system 10 provided in the embodiment of the present application directly enters the cooling shell 401 with liquid hydrogen as a heat exchange medium, absorbs the heat of the motor 40 , the temperature of the liquid hydrogen increases, and at the same time the motor 40 The temperature of the motor is reduced, so that the temperature of the motor is gradually reduced to below -150 °C, and it enters a superconducting state. The liquid hydrogen enters the stack heat exchanger 30 as a heat exchange medium to absorb heat. The fuel cell power system 10 causes the liquid hydrogen to absorb heat twice. The gasification efficiency of the liquid hydrogen is higher. Further, the fuel cell power system 10 enables liquid hydrogen to directly participate in heat exchange as a heat exchange medium, without the need for additional heat exchangers, thereby realizing a lightweight design.

所述燃料电池动力系统10采用所述液氢罐50代替气态罐,使得整个系统单位质量上对应的储能增加。所述系统的储氢质量密度可以从5%提高到10%至15%水平。The fuel cell power system 10 uses the liquid hydrogen tank 50 to replace the gaseous tank, so that the corresponding energy storage per unit mass of the entire system is increased. The hydrogen storage mass density of the system can be increased from 5% to 10% to 15% level.

在一个实施例中,所述电机40用于驱动无人机飞行。In one embodiment, the motor 40 is used to drive the drone to fly.

在一个实施例中,所述电机40为超低温的准超导电机。电机的能量损耗主要由于内部铜损、铁损、机械损耗与杂散损耗造成的。对于无人机飞行等工作场景,电机转速相对较低,能量损耗主要以铜损为主。电机长时间工作,温度升高。电机内部的铜绕组的温度升高,内阻增大。电机发热损耗能量,工作效率降低。所述燃料电池动力系统10通过液态氢直接作为热交换介质为所述电机40降温至超导温度,降低了铜绕组内阻,进而提高所述电机40的工作效率。In one embodiment, the motor 40 is an ultra-low temperature quasi-superconducting motor. The energy loss of the motor is mainly caused by the internal copper loss, iron loss, mechanical loss and stray loss. For working scenarios such as drone flight, the motor speed is relatively low, and the energy loss is mainly copper loss. When the motor works for a long time, the temperature rises. The temperature of the copper winding inside the motor increases, and the internal resistance increases. The motor heats up and loses energy, reducing the work efficiency. The fuel cell power system 10 directly uses liquid hydrogen as a heat exchange medium to cool the motor 40 to a superconducting temperature, thereby reducing the internal resistance of the copper winding, thereby improving the working efficiency of the motor 40 .

在一个实施例中,所述燃料电池动力系统10还包括第一储液装置310和第一电子泵320。所述第一储液装置310连接于所述待冷液出口302与所述冷水进口203之间。所述第一储液装置310用于储存进入所述电池堆20的水。所述第一电子泵320连接于所述第一储液装置310与所述冷水进口203之间。所述第一电子泵320为循环水提供动力。In one embodiment, the fuel cell power system 10 further includes a first liquid storage device 310 and a first electronic pump 320 . The first liquid storage device 310 is connected between the to-be-cooled liquid outlet 302 and the cold water inlet 203 . The first liquid storage device 310 is used to store water entering the battery stack 20 . The first electronic pump 320 is connected between the first liquid storage device 310 and the cold water inlet 203 . The first electronic pump 320 provides power for circulating water.

在一个实施例中,所述燃料电池动力系统10还包括第一减压阀80。所述第一减压阀80设置于所述冷却液出口304与所述氢气入口201之间。所述第一减压阀80避免所述氢气的压力过高,保证所述电池堆20的安全运行。In one embodiment, the fuel cell power system 10 further includes a first pressure relief valve 80 . The first pressure reducing valve 80 is disposed between the cooling liquid outlet 304 and the hydrogen inlet 201 . The first pressure reducing valve 80 prevents the pressure of the hydrogen from being too high, and ensures the safe operation of the battery stack 20 .

现有技术中,液氢存储罐采用双层的储罐储存液态氢,以满足绝热要求,保证安全。In the prior art, the liquid hydrogen storage tank adopts a double-layer storage tank to store liquid hydrogen to meet the thermal insulation requirements and ensure safety.

在一个实施例中,所述液氢罐50为单层壳体结构。所述燃料电池动力系统10应用于无人机。在飞行前,所述液氢罐50被补充液态氢。所述液氢罐50仅在飞行时储存。在无人机不飞行时,所述液态罐50不储存液态氢。因此,所述液态罐50并不用于运输。且在无人机飞行过程中,环境吸热气化的液氢被快速消耗。所述液氢罐50采用所述单层壳体结构,能够满足散热需求,适用于无人机飞行器这一特定场景。In one embodiment, the liquid hydrogen tank 50 is a single-layer shell structure. The fuel cell power system 10 is applied to an unmanned aerial vehicle. Before flight, the liquid hydrogen tank 50 is replenished with liquid hydrogen. The liquid hydrogen tank 50 is only stored during flight. When the drone is not flying, the liquid tank 50 does not store liquid hydrogen. Therefore, the liquid tank 50 is not used for transportation. And during the flight of the UAV, the liquid hydrogen gasified by the heat absorption in the environment is rapidly consumed. The liquid hydrogen tank 50 adopts the single-layer shell structure, which can meet the heat dissipation requirements, and is suitable for the specific scenario of an unmanned aerial vehicle.

在一个实施例中,所述单层壳体结构的表面设置保温层。所述保温层减小热交换,减缓液氢汽化。In one embodiment, an insulating layer is provided on the surface of the single-layer shell structure. The thermal insulation layer reduces heat exchange and slows down the vaporization of liquid hydrogen.

针对所述燃料电池动力系统10,进行可行性分析:For the fuel cell power system 10, a feasibility analysis is performed:

在一个实施例中,所述燃料电池动力系统10的综合效率为50%,系统发出1kW·h电能,对应产生1kW·h的废热。In one embodiment, the overall efficiency of the fuel cell power system 10 is 50%, and the system generates 1 kW·h of electrical energy, corresponding to 1 kW·h of waste heat.

废热+电能总共消耗了2kW·h的能量。按照每1kg氢气33kW·h电进行估算,2kW·h的能量相当于约61g氢气的化学能。The waste heat + electricity consumes a total of 2kW·h of energy. According to the estimation of 33kW·h electricity per 1kg of hydrogen, the energy of 2kW·h is equivalent to the chemical energy of about 61g of hydrogen.

液态氢从所述液氢罐50到所述电池堆20应用需要经过相态转变和升温两个过程。The application of liquid hydrogen from the liquid hydrogen tank 50 to the battery stack 20 needs to go through two processes of phase transition and temperature increase.

相态转变过程中,相变吸热为3.93kW·h/kg。61g氢气需要约0.240kW·h电能。During the phase transition process, the phase transition endotherm is 3.93kW·h/kg. 61g of hydrogen requires about 0.240kW·h of electricity.

升温过程中,61g氢气从20K上升到293K(20℃)。氢气的热容为14.3kJ/(kg·K)。61g气氢所需要的总能量为0.066kW·h电能。During the heating process, 61 g of hydrogen gas rose from 20K to 293K (20°C). The heat capacity of hydrogen is 14.3 kJ/(kg·K). The total energy required for 61g of gas hydrogen is 0.066kW·h electric energy.

综上可知,使用液氢时,提供1kW·h对外电能,氢气的总吸热量约为0.30kW·h。To sum up, when using liquid hydrogen, 1kW·h of external power is provided, and the total heat absorption of hydrogen is about 0.30kW·h.

对于典型电机+电机控制系统,整体效率约为90%。每输入1kW·h能量,产生的废热约为0.1kW·h。For a typical motor + motor control system, the overall efficiency is about 90%. For every 1kW·h of energy input, the waste heat generated is about 0.1kW·h.

因此,所述燃料电池动力系统10每对外输出1kW·h能量,燃料电池系统产生1kW·h的废热,电机系统产生0.1kW·h废热,液氢系统总吸热0.3kW·h。液氢总吸热量可以覆盖电机系统产热,也可以覆盖部分燃料电池系统产热。Therefore, when the fuel cell power system 10 outputs 1kW·h of energy, the fuel cell system generates 1kW·h of waste heat, the motor system generates 0.1kW·h of waste heat, and the liquid hydrogen system absorbs 0.3kW·h of heat. The total heat absorption of liquid hydrogen can cover the heat generated by the motor system, and can also cover the heat generated by part of the fuel cell system.

电机的能量损耗主要由于内部铜损、铁损、机械损耗与杂散损耗造成的。对于无人机飞行等工作场景,电机转速相对较低,能量损耗主要以铜损为主。电机长时间工作,温度升高。电机内部的铜绕组的温度升高,内阻增大。电机发热损耗能量,工作效率降低。所述燃料电池动力系统10通过液氢对所述电机40降温至超导工作环境,降低了铜绕组内阻,进而提高所述电机40的工作效率。The energy loss of the motor is mainly caused by the internal copper loss, iron loss, mechanical loss and stray loss. For working scenarios such as drone flight, the motor speed is relatively low, and the energy loss is mainly copper loss. When the motor works for a long time, the temperature rises. The temperature of the copper winding inside the motor increases, and the internal resistance increases. The motor heats up and loses energy, reducing the work efficiency. The fuel cell power system 10 cools the motor 40 to a superconducting working environment by using liquid hydrogen, which reduces the internal resistance of the copper winding, thereby improving the working efficiency of the motor 40 .

只要系统开始工作,液氢就需要从换热系统吸热,同时降低电机温度。所述电机处于超导状态,提升所述电机输出效率。所述燃料电池动力系统10降低了大功率系统的散热负担。进一步,所述燃料电池动力系统10中液氢吸热降低了散热参数的最大散热能力设计要求,减少了换热部件,减轻了系统重量。As soon as the system starts working, the liquid hydrogen needs to absorb heat from the heat exchange system while reducing the motor temperature. The motor is in a superconducting state, which improves the output efficiency of the motor. The fuel cell power system 10 reduces the heat dissipation burden of the high-power system. Further, the heat absorption of liquid hydrogen in the fuel cell power system 10 reduces the design requirements for the maximum heat dissipation capacity of the heat dissipation parameters, reduces heat exchange components, and reduces the weight of the system.

请参见图2,本申请实施例提供一种燃料电池动力系统10包括电池堆20、电堆换热器30、电机40、液氢罐50、缓冲罐60和换热装置70。所述电池堆20包括氢气入口201、热水出口202、冷水进口203、电力输出口204。所述电堆换热器30包括待冷液进口301和待冷液出口302。所述待冷液进口301与所述热水出口202连通。所述待冷液出口302与所述冷水进口203连通。所述电机40与所述电力输出口204电连接。所述液氢罐50用于存储液态氢气。所述液氢罐50包括液氢出口501。所述缓冲罐60包括进液口601和出液口602。所述进液口601与所述液氢出口501连通。所述出液口602与所述氢气入口201连通。Referring to FIG. 2 , an embodiment of the present application provides a fuel cell power system 10 including a battery stack 20 , a stack heat exchanger 30 , a motor 40 , a liquid hydrogen tank 50 , a buffer tank 60 and a heat exchange device 70 . The battery stack 20 includes a hydrogen inlet 201 , a hot water outlet 202 , a cold water inlet 203 , and a power outlet 204 . The stack heat exchanger 30 includes a liquid inlet 301 to be cooled and an outlet 302 of the liquid to be cooled. The to-be-cooled liquid inlet 301 communicates with the hot water outlet 202 . The to-be-cooled liquid outlet 302 communicates with the cold water inlet 203 . The motor 40 is electrically connected to the power outlet 204 . The liquid hydrogen tank 50 is used for storing liquid hydrogen. The liquid hydrogen tank 50 includes a liquid hydrogen outlet 501 . The buffer tank 60 includes a liquid inlet 601 and a liquid outlet 602 . The liquid inlet 601 communicates with the liquid hydrogen outlet 501 . The liquid outlet 602 communicates with the hydrogen inlet 201 .

所述换热装置70包括闭环连通的第二储液装置710、第一换热器720、第二换热器730和第三换热器740。所述第二储液装置710用于储存热交换介质。所述第一换热器720用于与所述缓冲罐60热交换。所述第二换热器730用于与所述电堆换热器30热交换。所述第三换热器740用于与所述电机40热交换。The heat exchange device 70 includes a second liquid storage device 710 , a first heat exchanger 720 , a second heat exchanger 730 and a third heat exchanger 740 in closed-loop communication. The second liquid storage device 710 is used for storing heat exchange medium. The first heat exchanger 720 is used for heat exchange with the buffer tank 60 . The second heat exchanger 730 is used for heat exchange with the stack heat exchanger 30 . The third heat exchanger 740 is used for heat exchange with the motor 40 .

本申请实施例提供的所述燃料电池动力系统10通过所述第一换热器720吸收液氢的冷量,热交换介质降温,同时液态氢气转变为气态氢气。所述气态氢气供所述电池堆20反应生成电能。所述电池堆20的电能为所述电机40供电。所述电池堆20在反应过程中产生热量。所述热量由循环水带入所述电堆换热器30。低温的热交换介质先通过所述第二换热器730为循环水降温,再通过所述第三换热器740为所述电机40降温,使所述电机40高效工作。所述燃料电池动力系统10通过所述换热装置70实现内部冷量和热量互补,提高了所述燃料电池动力系统10内部能量利用效率。进一步的,所述燃料电池动力系统10减少了外部冷源和热源设置,实现轻量化设计。The fuel cell power system 10 provided in the embodiment of the present application absorbs the cold energy of liquid hydrogen through the first heat exchanger 720 , the heat exchange medium is cooled, and the liquid hydrogen is converted into gaseous hydrogen at the same time. The gaseous hydrogen is used for the reaction of the cell stack 20 to generate electrical energy. The electrical energy of the battery stack 20 supplies power to the motor 40 . The cell stack 20 generates heat during the reaction. The heat is brought into the stack heat exchanger 30 by circulating water. The low temperature heat exchange medium first cools the circulating water through the second heat exchanger 730 , and then cools the motor 40 through the third heat exchanger 740 , so that the motor 40 works efficiently. The fuel cell power system 10 realizes the complementation of internal cooling capacity and heat through the heat exchange device 70 , thereby improving the internal energy utilization efficiency of the fuel cell power system 10 . Further, the fuel cell power system 10 reduces the arrangement of external cooling sources and heat sources, and realizes a lightweight design.

在一个实施例中,所述第一换热器720、所述第二换热器730和所述第三换热器740分别为换热铜管。In one embodiment, the first heat exchanger 720 , the second heat exchanger 730 and the third heat exchanger 740 are heat exchange copper tubes, respectively.

所述电池堆20需要用气态的氢气作为反应物。所述第二储液装置710用于储存热交换介质。所述热交换介质在所述换热装置70内循环。所述第一换热器720缠绕于所述缓冲罐60的壳体的外表面。所述热交换介质通过所述第一换热器720吸收所述液氢罐50中液态氢的冷量。所述热交换介质的温度变低。所述第二换热器730缠绕设置于所述电堆换热器30。低温的所述热交换介质通过所述第二换热器730吸收所述电堆换热器30内介质的热量,为所述电堆换热器30内的介质降温。所述第三换热器740缠绕设置于所述电机40的表面。低温的所述热交换介质在进入所述第三换热器740,为所述电机40降温。The stack 20 requires gaseous hydrogen as a reactant. The second liquid storage device 710 is used for storing heat exchange medium. The heat exchange medium circulates in the heat exchange device 70 . The first heat exchanger 720 is wound around the outer surface of the shell of the buffer tank 60 . The heat exchange medium absorbs the cold energy of the liquid hydrogen in the liquid hydrogen tank 50 through the first heat exchanger 720 . The temperature of the heat exchange medium becomes lower. The second heat exchanger 730 is wound around the stack heat exchanger 30 . The low-temperature heat exchange medium absorbs the heat of the medium in the stack heat exchanger 30 through the second heat exchanger 730 to cool the medium in the stack heat exchanger 30 . The third heat exchanger 740 is wound on the surface of the motor 40 . The low-temperature heat exchange medium enters the third heat exchanger 740 to cool the motor 40 .

在一个实施例中,所述燃料电池动力系统10还包括第二电子泵750。所述第二电子泵750连接于所述第二储液装置710与所述第一换热器720之间。所述第二电子泵750用于为所述热交换介质在管路中的流通提供动力。在一个实施例中,所述燃料电池动力系统10还包括第一储液装置310与第一电子泵320。所述第一储液装置310连接于所述待冷液出口302与所述冷水进口203之间。所述第一储液装置310用于储存进入所述电池堆20的冷却水,所述第一电子泵320为循环水提供动力。二者配合将燃料电池工作生成的热量带出,对燃料电池进行冷却,带出的热在所述电堆换热器30进行换热,循环维持燃料电池工作温度。In one embodiment, the fuel cell power system 10 further includes a second electronic pump 750 . The second electronic pump 750 is connected between the second liquid storage device 710 and the first heat exchanger 720 . The second electronic pump 750 is used to provide power for the circulation of the heat exchange medium in the pipeline. In one embodiment, the fuel cell power system 10 further includes a first liquid storage device 310 and a first electronic pump 320 . The first liquid storage device 310 is connected between the to-be-cooled liquid outlet 302 and the cold water inlet 203 . The first liquid storage device 310 is used to store the cooling water entering the battery stack 20 , and the first electronic pump 320 provides power for circulating water. The two cooperate to take out the heat generated by the operation of the fuel cell to cool the fuel cell, and the taken-out heat is exchanged in the stack heat exchanger 30 to maintain the operating temperature of the fuel cell in a cycle.

在一个实施例中,所述换热装置70还包括第四换热器760。所述第四换热器760连接于所述第二换热器730与所述第三换热器740之间。所述燃料电池动力系统10还包括电机控制器410。所述电机控制器410与所述电机40的信号输入端400电连接。所述第四换热器760用于与所述电机控制器410交换热量。所述第四换热器760用于降低所述电机控制器410降温。In one embodiment, the heat exchange device 70 further includes a fourth heat exchanger 760 . The fourth heat exchanger 760 is connected between the second heat exchanger 730 and the third heat exchanger 740 . The fuel cell power system 10 also includes a motor controller 410 . The motor controller 410 is electrically connected to the signal input terminal 400 of the motor 40 . The fourth heat exchanger 760 is used for exchanging heat with the motor controller 410 . The fourth heat exchanger 760 is used to reduce the temperature of the motor controller 410 .

在一个实施例中,所述第二电子泵750的出口与所述第一换热器720的入口连通。所述热交换介质先进入所述第一换热器720吸收冷量,再顺次进入所述第二换热器730、所述第四换热器760和第三换热器740吸热。In one embodiment, the outlet of the second electronic pump 750 communicates with the inlet of the first heat exchanger 720 . The heat exchange medium first enters the first heat exchanger 720 to absorb cold energy, and then sequentially enters the second heat exchanger 730 , the fourth heat exchanger 760 and the third heat exchanger 740 to absorb heat.

所述热交换介质在所述第一换热器720内吸收冷量。所述热交换介质将热量传递给所述缓冲罐60。所述缓冲罐60内的液氢温度升高气化。所述热交换介质的温度降低。The heat exchange medium absorbs cold energy in the first heat exchanger 720 . The heat exchange medium transfers heat to the buffer tank 60 . The temperature of the liquid hydrogen in the buffer tank 60 increases and gasifies. The temperature of the heat exchange medium decreases.

低温的所述热交换介质先进入所述第二换热器730,用于为所述电堆换热器30内的水降温。所述电池堆20的循环水的温度比所述电机40的温度低。低温的所述热交换介质先进入所述第二换热器730,对所述电池堆20的循环水的降温效果更好。The low-temperature heat exchange medium first enters the second heat exchanger 730 for cooling the water in the stack heat exchanger 30 . The temperature of the circulating water of the battery stack 20 is lower than the temperature of the motor 40 . The low-temperature heat exchange medium first enters the second heat exchanger 730 , which has a better cooling effect on the circulating water of the battery stack 20 .

在应用中,所述热交换介质也可以先为所述电机40或所述电机控制器410降温,再为所述电池堆20的循环水降温。In application, the heat exchange medium may also cool the motor 40 or the motor controller 410 first, and then cool the circulating water of the battery stack 20 .

所述热交换介质还可以先为所述电机40、所述电机控制器410或所述电池堆20的循环水降温,升温后的所述热交换介质再对液氢加热。The heat exchange medium may also firstly cool the circulating water of the motor 40 , the motor controller 410 or the battery stack 20 , and then the heated heat exchange medium heats the liquid hydrogen.

现有技术中,电池系统中采用双层的储罐储存液态氢,以满足绝热要求,保证安全。In the prior art, a double-layer storage tank is used in the battery system to store liquid hydrogen to meet the thermal insulation requirements and ensure safety.

在一个实施例中,所述液氢罐50为单层壳体结构。In one embodiment, the liquid hydrogen tank 50 is a single-layer shell structure.

所述燃料电池动力系统10应用于无人机。在飞行前,所述液氢罐50被补充液态氢。所述液氢罐50仅在飞行时储存。在无人机不飞行时,所述液态罐50不储存液态氢。因此,所述液态罐50并不用于运输。且在无人机飞行过程中,液氢吸热逐渐减少,同时液氢及时被系统反应消耗。所述液氢罐50采用所述单层壳体结构,能够满足强度要求。The fuel cell power system 10 is applied to an unmanned aerial vehicle. Before flight, the liquid hydrogen tank 50 is replenished with liquid hydrogen. The liquid hydrogen tank 50 is only stored during flight. When the drone is not flying, the liquid tank 50 does not store liquid hydrogen. Therefore, the liquid tank 50 is not used for transportation. And during the flight of the UAV, the heat absorption of liquid hydrogen gradually decreases, and the liquid hydrogen is consumed by the system reaction in time. The liquid hydrogen tank 50 adopts the single-layer shell structure, which can meet the strength requirements.

以上所述实施例的各技术特征可以进行任意的组合,为使描述简洁,未对上述实施例中的各个技术特征所有可能的组合都进行描述,然而,只要这些技术特征的组合不存在矛盾,都应当认为是本说明书记载的范围。The technical features of the above-described embodiments can be combined arbitrarily. For the sake of brevity, all possible combinations of the technical features in the above-described embodiments are not described. However, as long as there is no contradiction between the combinations of these technical features, All should be regarded as the scope described in this specification.

以上所述实施例仅表达了本申请的几种实施方式,但并不能因此而理解为对本申请专利范围的限制。应当指出的是,对于本领域的普通技术人员来说,在不脱离本申请构思的前提下,还可以做出若干变形和改进,这些都属于本申请的保护范围。因此,本申请专利的保护范围应以所附权利要求为准。The above-mentioned embodiments only represent several embodiments of the present application, but should not be construed as limiting the scope of the present application. It should be pointed out that for those skilled in the art, without departing from the concept of the present application, several modifications and improvements can be made, which all belong to the protection scope of the present application. Therefore, the scope of protection of the patent of the present application shall be subject to the appended claims.

Claims (10)

1. A fuel cell power system, wherein the fuel cell power system is used for unmanned aerial vehicle, the fuel cell power system includes:
a cell stack (20), the cell stack (20) comprising a hydrogen inlet (201), a hot water outlet (202), a cold water inlet (203), an electrical power outlet (204);
the galvanic pile heat exchanger (30) comprises a cooling liquid inlet (303), a cooling liquid outlet (304), a liquid to be cooled inlet (301) and a liquid to be cooled outlet (302), wherein the liquid to be cooled inlet (301) is communicated with the hot water outlet (202), and the liquid to be cooled outlet (302) is communicated with the cold water inlet (203);
an electric motor (40), the power outlet (204) being electrically connected to the electric motor (40), the electric motor (40) comprising a cooling enclosure (401), the cooling enclosure (401) comprising a first inlet (402) and a first outlet (403);
liquid hydrogen jar (50), liquid hydrogen jar (50) include liquid hydrogen export (501), liquid hydrogen export (501) with first import (402) intercommunication, first export (403) with coolant liquid inlet (303) intercommunication, coolant liquid outlet (304) with hydrogen entry (201) intercommunication, liquid hydrogen jar (50) are single-deck shell structure.
2. The fuel cell power system of claim 1, further comprising:
a first liquid storage device (310) connected between the outlet (302) of the liquid to be cooled and the cold water inlet (203);
a first electronic pump (320) connected between the first reservoir (310) and the cold water inlet (203).
3. The fuel cell power system of claim 1, further comprising:
a first pressure reducing valve (80), the first pressure reducing valve (80) being disposed between the coolant outlet (304) and the hydrogen gas inlet (201).
4. The fuel cell power system of claim 1, wherein the surface of the single shell structure is provided with insulation.
5. A fuel cell power system according to claim 1, wherein the electric machine (40) is a superconducting electric machine, and the superconducting operating state is achieved by liquid hydrogen cooling.
6. A fuel cell power system, wherein the fuel cell power system is used for unmanned aerial vehicle, the fuel cell power system includes:
a cell stack (20), the cell stack (20) comprising a hydrogen inlet (201), a hot water outlet (202), a cold water inlet (203), an electrical power outlet (204);
the galvanic pile heat exchanger (30) comprises a liquid to be cooled inlet (301) and a liquid to be cooled outlet (302), the liquid to be cooled inlet (301) is communicated with the hot water outlet (202), and the liquid to be cooled outlet (302) is communicated with the cold water inlet (203);
a motor (40) electrically connected to the power outlet (204);
the liquid hydrogen tank (50) is used for storing liquid hydrogen, the liquid hydrogen tank (50) comprises a liquid hydrogen outlet (501), and the liquid hydrogen tank (50) is of a single-layer shell structure;
a buffer tank (60), wherein the buffer tank (60) comprises a liquid inlet (601) and a liquid outlet (602), the liquid inlet (601) is communicated with the liquid hydrogen outlet (501), and the liquid outlet (602) is communicated with the hydrogen inlet (201);
the heat exchange device (70) comprises a second liquid storage device (710), a first heat exchanger (720), a second heat exchanger (730) and a third heat exchanger (740) which are communicated in a closed loop, the second liquid storage device (710) is used for storing a heat exchange medium, the first heat exchanger (720) is used for exchanging heat with the buffer tank (60), the second heat exchanger (730) is used for exchanging heat with the pile heat exchanger (30), and the third heat exchanger (740) is used for exchanging heat with the motor (40).
7. The fuel cell power system of claim 6, further comprising:
a first liquid storage device (310) connected between the outlet (302) of the liquid to be cooled and the cold water inlet (203);
a first electronic pump (320) connected between the first reservoir (310) and the cold water inlet (203).
8. The fuel cell power system of claim 6, further comprising:
and the second electronic pump (750) is connected between the second liquid storage device (710) and the first heat exchanger (720) and used for circulating a cooling medium.
9. The fuel cell power system as defined in claim 8, wherein an outlet of the second electronic pump (750) communicates with an inlet of the first heat exchanger (720).
10. The fuel cell power system according to claim 6, wherein the heat exchanging means (70) further comprises a fourth heat exchanger (760), the fourth heat exchanger (760) being connected between the second heat exchanger (730) and the third heat exchanger (740), the fuel cell power system (10) further comprising:
a motor controller (410), the motor controller (410) being electrically connected to a signal input (400) of the motor (40), the fourth heat exchanger (760) being configured to exchange heat with the motor controller (410).
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