WO2017117918A1 - Temperature control system and method for dc-dc boost converter of fuel cell automobile - Google Patents

Temperature control system and method for dc-dc boost converter of fuel cell automobile Download PDF

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Publication number
WO2017117918A1
WO2017117918A1 PCT/CN2016/085894 CN2016085894W WO2017117918A1 WO 2017117918 A1 WO2017117918 A1 WO 2017117918A1 CN 2016085894 W CN2016085894 W CN 2016085894W WO 2017117918 A1 WO2017117918 A1 WO 2017117918A1
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WIPO (PCT)
Prior art keywords
temperature
boost converter
methanol
control system
hydrogen
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PCT/CN2016/085894
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French (fr)
Chinese (zh)
Inventor
向华
Original Assignee
广东合即得能源科技有限公司
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Publication of WO2017117918A1 publication Critical patent/WO2017117918A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60LPROPULSION OF ELECTRICALLY-PROPELLED VEHICLES; SUPPLYING ELECTRIC POWER FOR AUXILIARY EQUIPMENT OF ELECTRICALLY-PROPELLED VEHICLES; ELECTRODYNAMIC BRAKE SYSTEMS FOR VEHICLES IN GENERAL; MAGNETIC SUSPENSION OR LEVITATION FOR VEHICLES; MONITORING OPERATING VARIABLES OF ELECTRICALLY-PROPELLED VEHICLES; ELECTRIC SAFETY DEVICES FOR ELECTRICALLY-PROPELLED VEHICLES
    • B60L50/00Electric propulsion with power supplied within the vehicle
    • B60L50/50Electric propulsion with power supplied within the vehicle using propulsion power supplied by batteries or fuel cells
    • B60L50/70Electric propulsion with power supplied within the vehicle using propulsion power supplied by batteries or fuel cells using power supplied by fuel cells
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B60VEHICLES IN GENERAL
    • B60LPROPULSION OF ELECTRICALLY-PROPELLED VEHICLES; SUPPLYING ELECTRIC POWER FOR AUXILIARY EQUIPMENT OF ELECTRICALLY-PROPELLED VEHICLES; ELECTRODYNAMIC BRAKE SYSTEMS FOR VEHICLES IN GENERAL; MAGNETIC SUSPENSION OR LEVITATION FOR VEHICLES; MONITORING OPERATING VARIABLES OF ELECTRICALLY-PROPELLED VEHICLES; ELECTRIC SAFETY DEVICES FOR ELECTRICALLY-PROPELLED VEHICLES
    • B60L58/00Methods or circuit arrangements for monitoring or controlling batteries or fuel cells, specially adapted for electric vehicles
    • B60L58/30Methods or circuit arrangements for monitoring or controlling batteries or fuel cells, specially adapted for electric vehicles for monitoring or controlling fuel cells
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00Fuel cells; Manufacture thereof
    • H01M8/06Combination of fuel cells with means for production of reactants or for treatment of residues
    • H01M8/0606Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants
    • H01M8/0612Combination of fuel cells with means for production of reactants or for treatment of residues with means for production of gaseous reactants from carbon-containing material
    • H01M8/0618Reforming processes, e.g. autothermal, partial oxidation or steam reforming
    • 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
    • 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
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T90/00Enabling technologies or technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02T90/40Application of hydrogen technology to transportation, e.g. using fuel cells

Definitions

  • the present invention relates to the field of fuel cell vehicles, and in particular, to a DC-DC boost converter temperature control system and method for a fuel cell vehicle.
  • An electric vehicle is a vehicle that is driven by a vehicle power source and drives the wheels with a motor.
  • Electric vehicles include pure electric vehicles, hybrid vehicles and fuel cell vehicles.
  • Fuel cell A car is an electric car equipped with a fuel cell as a power source for obtaining a driving force.
  • the fuel cell of a fuel cell car is used for electrochemical reaction of hydrogen and oxygen in the air to generate electric energy.
  • the fuel cell generates electricity with a DC voltage of 15 to 35 V, but the power required by the automobile motor is usually 200 to 750 V DC. Therefore, the fuel cell vehicle also needs to be equipped with a DC-DC boost converter for the fuel cell.
  • the low voltage DC voltage boost is converted to the high voltage DC voltage required by the automotive motor.
  • the DC-DC boost converter of a fuel cell vehicle usually emits a large amount of heat during operation, and therefore, temperature control of the DC-DC boost converter is critical.
  • the temperature control device of the DC-DC boost converter usually adopts an air-cooled heat sink, but the air-cooled heat sink of the DC-DC boost converter has at least the following defects: First, the air-cooled heat sink The cooling fan has high noise, which is not conducive to the noise reduction of the fuel cell system. Second, due to the slow heat dissipation of the air, the heat dissipation efficiency of the air-cooled heat sink is low. When the DC-DC boost converter has power adjustment, it is easy.
  • the peak temperature occurs, destroying the DC-DC boost converter; Third, the cooling fan of the air-cooled radiator itself needs power supply to maintain operation, and the energy consumption is high; fourth, the heat generated by the DC-DC boost converter is The cooling fan blows away, wasting heat energy; Fifth, the heat discharged by the D C-DC boost converter is likely to adversely affect the internal electronic circuit of the car.
  • the cooling circulation system needs to be provided with a water tank, a booster pump and a radiator.
  • the booster pump drives the water in the water tank to flow through the DC/DC converter and the radiator.
  • the radiator works (hidden Containing fans), cooling; this not only increases equipment costs, takes up a lot of space, but also requires the energy itself to keep running;
  • the heat generated by the DC-DC boost converter is still It is wasted by the heat sink and wastes heat.
  • the heat discharged by the DC-DC boost converter is still very easy to adversely affect the internal electronic circuit of the car.
  • the technical problem to be solved by the present invention is to provide a DC-DC boost converter temperature control system for a fuel cell vehicle, and the DC-DC boost converter temperature control system noise for the above-mentioned deficiencies in the prior art.
  • Low, good heat dissipation, low energy consumption, small footprint, and fuel cell vehicles can effectively utilize the heat generated by the DC-DC boost converter, without affecting the fuel cell due to the heat output of the DC-DC boost converter
  • the other electronic circuits of the car work.
  • the present invention also provides a temperature control method for the DC-DC boost converter temperature control system.
  • a DC-DC boost converter temperature control system for a fuel cell vehicle comprising:
  • a DC-DC boost converter for converting low-voltage direct current output from a fuel cell into high-voltage direct current required for an automobile motor; the DC-DC boost converter having a methanol temperature controller, wherein the methanol liquid is During the pumping process of the transfer pump, the methanol temperature controller is passed to control the operating temperature of the DC-DC boost converter; [0011] a hydrogen production system for hydrogen production from methanol, and the hydrogen produced is supplied to the fuel cell. ;
  • a fuel cell for electrochemical reaction of hydrogen and oxygen in the air to generate low-voltage direct current, the low voltage
  • the DC power is converted into high voltage direct current through a DC-DC boost converter and supplied to the automobile motor;
  • the DC-DC boost converter temperature control system further includes a three-way regulating diverter valve and a three-way confluence valve, wherein the inlet port of the three-way regulating diverter valve is in communication with the transfer pump,
  • the methanol liquid pumped by the pump is divided into two fluids through the three-way regulating diverter valve, wherein the first fluid passes through the methanol temperature controller of the DC-DC boost converter and enters the three-way confluence valve, and the second fluid directly Enter the three-way confluence valve; the two fluids are combined in the three-way confluence valve and sent to the hydrogen production system.
  • the DC-DC boost converter is provided with a temperature sensor, and the temperature sensor is electrically connected to the control system.
  • the hydrogen production system comprises a heat exchanger and a reformer
  • the heat exchanger is installed on a conveying pipe of a methanol liquid
  • the methanol liquid is in the heat exchanger
  • the high temperature hydrogen gas is outputted from the reformer.
  • the reformer is provided with a reforming chamber, a heating device and a hydrogen purifying device, and the heating device provides heat energy of a temperature of 350-570 ° C for the reforming chamber;
  • the reforming chamber is provided with a catalyst 1J, and in the reforming chamber, a hydrogenation reaction of methanol and water occurs to produce a high-temperature mixed gas mainly composed of carbon dioxide and hydrogen; and the reforming chamber is connected with a hydrogen purifying device.
  • the pipeline connection, all or part of the connecting pipeline is disposed in the reforming chamber, and can continue to heat the high-temperature mixed gas output from the reforming chamber through the high temperature in the reforming chamber;
  • the connecting pipeline serves as a reforming chamber and a hydrogen purifying device
  • the buffering is such that the temperature of the high temperature mixed gas output from the reforming chamber is the same as or close to the temperature of the hydrogen purifying device; hydrogen gas is obtained from the gas producing end of the hydrogen purifying device, After air through the heat exchanger to the output of the fuel cell.
  • the heating device of the reformer is an electric heater or an electromagnetic heater or a hydrogen fuel chamber.
  • a temperature control method for a DC-DC boost converter temperature control system of a fuel cell vehicle comprising the following steps:
  • the methanol liquid in the methanol container flows through the methanol temperature controller of the DC-DC boost converter under the pumping force of the transfer pump, and the methanol liquid flows through the methanol temperature controller. Take away the heat in the DC-DC boost converter and raise the temperature of the methanol liquid;
  • the methanol liquid pumped by the pump is divided into two channels by a three-way regulating diverter valve, wherein the first channel fluid enters the tee through the methanol temperature controller of the DC-DC boost converter Confluence valve, the second fluid directly enters the three-way confluence valve; the two fluids are combined in the three-way confluence valve and sent to the hydrogen production system; the control system adjusts the diversion through the three-way according to the temperature of the DC-DC boost converter The valve controls the flow of methanol liquid flowing through the methanol temperature controller.
  • the control system controls the three-way regulating diverter valve to increase the flow rate of the first fluid, and the flow rate of the second fluid is Corresponding reduction;
  • the control system controls the three-way regulating diverter valve to reduce the flow of the first fluid, and the flow of the second fluid is correspondingly increased.
  • the DC-DC boost converter is provided with a temperature sensor that feeds back a temperature signal of the DC-DC boost converter to the control system, and the control system adjusts according to the temperature signal.
  • the beneficial effects of the present invention are as follows: 1.
  • the DC-DC boost converter of the present invention uses a methanol temperature controller to dissipate heat, and does not need to additionally provide a booster pump and a fan, which occupies small space and is noise-free, and is beneficial to the entire fuel.
  • the battery layout and noise reduction of the battery car Second, the methanol temperature controller of the DC-DC boost converter skillfully uses the methanol liquid to take away the heat generated by the DC-DC boost converter, without the need to additionally provide a liquid cooling fan.
  • the methanol liquid takes away the heat generated by the DC-DC boost converter, which can raise the temperature of the methanol liquid, so that the heat generated by the DC-DC boost converter is skillfully utilized; Moreover, the heat generated by the DC-DC boost converter is utilized, so that the DC-DC boost converter does not discharge heat to the interior of the fuel cell vehicle, thereby ensuring the operational stability of the fuel cell vehicle.
  • a three-way regulating diverter valve and a three-way confluence valve are provided, so that the control system of the present invention can adjust the flow of the methanol temperature controller according to the temperature signal of the DC-DC boost converter.
  • the methanol liquid flow rate is controlled to be stable and reliable by controlling the temperature of the DC-DC boost converter within a set range.
  • DRAWINGS 1 is a block diagram showing the overall structure of the present invention.
  • FIG. 2 is a block diagram showing the overall structure of a preferred embodiment of the present invention.
  • the present invention is a DC-DC boost converter temperature control system for a fuel cell vehicle, including
  • the methanol container 1 stores therein a methanol-based liquid, preferably an aqueous methanol solution;
  • a transfer pump 2 for pumping the methanol liquid in the methanol container 1 to the hydrogen production system through the delivery pipe;
  • a DC-DC boost converter 3 for converting the low voltage direct current output of the fuel cell 5
  • the high-voltage direct current required for the automobile motor 7, the low-voltage direct current is usually 15 ⁇ 35V direct current, the high-voltage direct current is usually 200 ⁇ 750V direct current;
  • the DC-DC boost converter 3 has a methanol temperature controller 31, The methanol liquid flows through the methanol temperature controller 31 during the pumping process of the transfer pump 2 to control the operating temperature of the DC-DC boost converter 3;
  • a hydrogen production system for hydrogen production from methanol, the hydrogen produced is supplied to the fuel cell 6;
  • PEM proton exchange membrane
  • control system for controlling the operation of the transfer pump 2, the DC-DC boost converter 3, the hydrogen production system, and the fuel cell 6.
  • the DC-DC boost converter temperature control system further includes a three-way regulating diverter valve 8 and a three-way confluence valve 9, the three-way regulating diverter valve 8 inlet and delivery
  • the pump 2 is in communication, and the methanol liquid pumped by the pump 2 is divided into two channels by the three-way regulating diverter valve 8, wherein the first channel fluid passes through the methanol temperature controller 31 of the DC-DC boost converter 3.
  • the second fluid directly enters the three-way confluence valve 9; the two fluids are merged in the three-way confluence valve 9, and then sent to the hydrogen production system, through the control of the three-way regulating diverter valve 8,
  • the surface makes the temperature of the DC-DC boost converter within the set range, stable and reliable.
  • the DC-DC boost converter 3 is provided with a temperature sensor (not shown), and the temperature sensor is electrically connected to the control system, so that the control system can monitor the DC-DC boost conversion.
  • the hydrogen production system includes a heat exchanger 5 and a reformer 4, the heat exchanger 5 is installed on a conveying pipe of a methanol liquid, and the methanol liquid is in the heat exchanger 5,
  • the high-temperature hydrogen outputted by the reformer 4 performs heat exchange, the temperature of the methanol liquid rises, and the temperature of the hydrogen gas decreases.
  • the reformer 4 is provided with a reforming chamber 41, a heating device 42, and a hydrogen purifying device 43, wherein the heating device 42 is
  • the reforming chamber 41 provides thermal energy at a temperature of 350-570 ° C; the reforming chamber 41 is provided with a catalyst, and under the action of the catalyst, a methanol cracking reaction and a carbon monoxide shift reaction are generated to generate hydrogen gas and carbon dioxide, which is more than one.
  • reaction equation is: (l) CH 3 OH ⁇ CO + 2H 2 , (2) H 2 0 + CO ⁇ CO 2 + H 2 , (3) CH 3 OH + H 2 0 ⁇ C0 2 +3H 2 , a high-temperature mixed gas mainly composed of carbon dioxide and hydrogen; the reforming chamber 41 and the hydrogen purifying device 43 are connected by a connecting pipe, and all or part of the connecting pipe is set in the reforming In the chamber 41, the heating can be continued from the reforming chamber 41 by the high temperature in the reforming chamber 41.
  • the connecting line acts as a buffer between the reforming chamber 41 and the hydrogen purifying device 43, so that the temperature of the high-temperature mixed gas output from the reforming chamber 41 is the same as or close to the temperature of the hydrogen purifying device 43; Hydrogen is obtained from the gas producing end of the hydrogen purifying unit 43, and the hydrogen is supplied to the fuel cell 6 via the heat exchanger 5.
  • the heating device 42 of the reformer 4 may be an electric heater or an electromagnetic heater or a hydrogen fuel chamber, preferably an electromagnetic heater.
  • an electric heater or an electromagnetic heater or a hydrogen fuel chamber, preferably an electromagnetic heater.
  • the temperature control method of the DC-DC boost converter temperature control system of the fuel cell automobile includes the following steps: [0038] (1) The methanol liquid in the methanol container flows under the pumping force of the transfer pump Through the methanol temperature controller of the DC-DC boost converter, the methanol liquid takes away the heat in the DC-DC boost converter during the flow through the methanol temperature controller, and raises the temperature of the methanol liquid;
  • the methanol liquid pumped by the transfer pump is divided into two channels by a three-way regulating diverter valve, wherein the first path fluid passes through the methanol temperature controller of the DC-DC boost converter.
  • the second fluid After entering the three links Confluence valve, the second fluid directly enters the three-way confluence valve; the two fluids are combined in the three-way confluence valve and sent to the hydrogen production system; the control system adjusts the diversion through the three-way according to the temperature of the DC-DC boost converter
  • the valve controls the flow of methanol liquid flowing through the methanol temperature controller.
  • the control system controls the three-way regulating diverter valve to increase the flow rate of the first fluid, and the flow rate of the second fluid is Corresponding reduction;
  • the control system controls the three-way regulating diverter valve to reduce the flow of the first fluid, and the flow of the second fluid is correspondingly increased.
  • the DC-DC boost converter is provided with a temperature sensor, and the temperature sensor actually feeds back a temperature signal of the DC-DC boost converter to the control system, and the control system adjusts according to the temperature signal.
  • the present invention is a fuel cell vehicle DC-DC boost converter temperature control system and method, the DC-DC boost converter temperature control system has low noise, good heat dissipation effect, low energy consumption, and small space occupation And the fuel cell vehicle can effectively utilize the heat generated by the DC-DC boost converter, and does not affect the operation of other electronic circuits of the fuel cell vehicle due to the discharge of the heat of the DC-DC boost converter. Therefore, it has industrial applicability.

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Abstract

A temperature control system and method for a DC-DC boost converter of a fuel cell automobile. The temperature control system comprises a methyl alcohol container (1) storing liquid which is mainly methyl alcohol, a conveying pump (2) used for pumping methyl alcohol liquid in the methyl alcohol container (1) into a hydrogen preparation system by means of a conveying pipeline pump, and a DC-DC boost converter (3) used for converting low-voltage direct current output by a fuel cell (6) into high-voltage direct current required by an automobile motor (7). The DC-DC boost converter (3) is provided with a methyl alcohol temperature controller (31), and the methyl alcohol liquid flows through the methyl alcohol temperature controller (31) during a pumping process of the conveying pump (2) so as to control the working temperature of the DC-DC boost converter (3). The system and method are low in noise, have a good cooling effect, are low in energy consumption and occupy little space, and heat generated by the DC-DC boost converter (3) can be effectively utilized by a fuel cell automobile. Thus, the working and running of other electronic circuits of the fuel cell automobile will not be influenced by the fact that the heat of the DC-DC boost converter (3) is discharged.

Description

说明书 发明名称:燃料电池汽车的 DC-DC升压转换器控温系统及方法 技术领域  Title: Inventor Name: DC-DC Boost Converter Temperature Control System and Method for Fuel Cell Vehicles
[0001] 本发明涉及燃料电池汽车技术领域, 特别涉及一种燃料电池汽车的 DC-DC升压 转换器控温系统及方法。  [0001] The present invention relates to the field of fuel cell vehicles, and in particular, to a DC-DC boost converter temperature control system and method for a fuel cell vehicle.
背景技术  Background technique
[0002] 目前, 绝大部分汽车都以汽油、 柴油为燃料, 不仅消耗了大量的石油资源, 而 且汽车尾气造成了严重的大气污染。 为应对此资源问题和环境问题, 电动汽车 的幵发变得非常重要。 电动汽车是指以车载电源为动力, 用电机驱动车轮行驶 的车辆。 电动汽车包括纯电动汽车、 混合动力汽车和燃料电池汽车。 燃料电池 汽车是指装备了燃料电池作为获得驱动力的电源的电动汽车, 燃料电池汽车的 燃料电池用于氢气及空气中的氧气发生电化学反应产生电能。 燃料电池产生的 电通常为 15〜35V的直流电压, 但汽车马达所需要的电通常为 200〜750V的直流 电压, 因此, 燃料电池汽车还需要配置 DC-DC升压转换器, 以便将燃料电池的 低压直流电压升压转换为汽车马达所需要的高压直流电压。  [0002] At present, most of the cars are fueled by gasoline and diesel, which not only consume a large amount of petroleum resources, but also cause serious air pollution from automobile exhaust. In response to this resource issue and environmental issues, the emergence of electric vehicles has become very important. An electric vehicle is a vehicle that is driven by a vehicle power source and drives the wheels with a motor. Electric vehicles include pure electric vehicles, hybrid vehicles and fuel cell vehicles. Fuel cell A car is an electric car equipped with a fuel cell as a power source for obtaining a driving force. The fuel cell of a fuel cell car is used for electrochemical reaction of hydrogen and oxygen in the air to generate electric energy. The fuel cell generates electricity with a DC voltage of 15 to 35 V, but the power required by the automobile motor is usually 200 to 750 V DC. Therefore, the fuel cell vehicle also needs to be equipped with a DC-DC boost converter for the fuel cell. The low voltage DC voltage boost is converted to the high voltage DC voltage required by the automotive motor.
[0003] 燃料电池汽车的 DC-DC升压转换器在工作吋, 通常会散发大量热量, 因此, 对 DC-DC升压转换器的温度控制显得非常关键。 在现有技术中, DC-DC升压转换 器的温度控制装置通常采用风冷散热器, 但是 DC-DC升压转换器的风冷散热器 至少具有以下缺陷: 其一、 风冷散热器的散热风扇噪音高, 不利于燃料电池系 统的降噪; 其二、 由于空气的散热速度较慢, 使得风冷散热器的散热效率较低 , 当 DC-DC升压转换器有功率调整吋, 易出现尖峰温度, 破坏 DC-DC升压转换 器; 其三、 风冷散热器的散热风扇本身需要电能供给才能维持运转, 耗能高; 其四、 DC-DC升压转换器所产生的热量被散热风扇吹走, 浪费了热能; 其五、 D C-DC升压转换器排出的热量易对汽车内部电子电路造成不利影响。  [0003] The DC-DC boost converter of a fuel cell vehicle usually emits a large amount of heat during operation, and therefore, temperature control of the DC-DC boost converter is critical. In the prior art, the temperature control device of the DC-DC boost converter usually adopts an air-cooled heat sink, but the air-cooled heat sink of the DC-DC boost converter has at least the following defects: First, the air-cooled heat sink The cooling fan has high noise, which is not conducive to the noise reduction of the fuel cell system. Second, due to the slow heat dissipation of the air, the heat dissipation efficiency of the air-cooled heat sink is low. When the DC-DC boost converter has power adjustment, it is easy. The peak temperature occurs, destroying the DC-DC boost converter; Third, the cooling fan of the air-cooled radiator itself needs power supply to maintain operation, and the energy consumption is high; fourth, the heat generated by the DC-DC boost converter is The cooling fan blows away, wasting heat energy; Fifth, the heat discharged by the D C-DC boost converter is likely to adversely affect the internal electronic circuit of the car.
[0004] 随着液冷散热器技术的发展, 液冷散热器也逐渐应用于于燃料电池汽车的 DC- DC升压转换器。 中国专利 200810246572.2 (申请日: 2008-12-25, 申请人: 清华 大学) 公幵了一种燃料电池城市客车车载冷却循环系统, 该系统水箱、 散热器 、 增压泵、 DC/DC变换器、 辅助 DC/DC变换器、 电机控制器、 电机通过钢丝耐 压水管连接实现冷却系统水路连接, 并由控制系统对冷却系统的增压泵进行控 制, 实现水路循环, 其散热效率较好。 [0004] With the development of liquid-cooled heat sink technology, liquid-cooled heat sinks have also been gradually applied to DC-DC boost converters of fuel cell vehicles. Chinese patent 200810246572.2 (application date: 2008-12-25, applicant: Tsinghua University) publicly listed a fuel cell city bus car cooling circulation system, the system water tank, radiator The booster pump, the DC/DC converter, the auxiliary DC/DC converter, the motor controller, and the motor are connected by a steel pressure pipe to realize the water connection of the cooling system, and the control system controls the boosting pump of the cooling system to realize Water circulation, its heat dissipation efficiency is better.
[0005] 然而, 上述专利 200810246572.2所公幵的冷却循环系统还具有如下缺陷: 其一[0005] However, the cooling cycle system disclosed in the above-mentioned patent 200810246572.2 has the following drawbacks:
、 该冷却循环系统需要设置水箱、 增压泵和散热器, 增压泵驱动水箱中的水流 经 DC/DC变换器及散热器, 当 DC/DC变换器达到一定温度后, 散热器工作 (隐 含有风扇) , 冷却; 这样一来, 不仅增加了设备成本、 占用了较大空间, 而且 这些设备本身也需要耗费能量才能维持运转; 其二、 DC-DC升压转换器所产生 的热量仍然被散热器带走, 浪费了热能; 其三、 DC-DC升压转换器排出的热量 仍然很容易对汽车内部电子电路造成不利影响。 The cooling circulation system needs to be provided with a water tank, a booster pump and a radiator. The booster pump drives the water in the water tank to flow through the DC/DC converter and the radiator. When the DC/DC converter reaches a certain temperature, the radiator works (hidden Containing fans), cooling; this not only increases equipment costs, takes up a lot of space, but also requires the energy itself to keep running; second, the heat generated by the DC-DC boost converter is still It is wasted by the heat sink and wastes heat. Third, the heat discharged by the DC-DC boost converter is still very easy to adversely affect the internal electronic circuit of the car.
技术问题  technical problem
[0006] 本发明要解决的技术问题是针对上述现有技术中的不足, 提供一种燃料电池汽 车的 DC-DC升压转换器控温系统, 该 DC-DC升压转换器控温系统噪音低、 散热 效果好、 耗能低, 占用空间小, 并且燃料电池汽车能够有效利用 DC-DC升压转 换器所产生的热量, 不会因为 DC-DC升压转换器热量的排出而影响燃料电池汽 车的其他电子电路工作运转。 为此, 本发明还要提供一种该 DC-DC升压转换器 控温系统的控温方法。  [0006] The technical problem to be solved by the present invention is to provide a DC-DC boost converter temperature control system for a fuel cell vehicle, and the DC-DC boost converter temperature control system noise for the above-mentioned deficiencies in the prior art. Low, good heat dissipation, low energy consumption, small footprint, and fuel cell vehicles can effectively utilize the heat generated by the DC-DC boost converter, without affecting the fuel cell due to the heat output of the DC-DC boost converter The other electronic circuits of the car work. To this end, the present invention also provides a temperature control method for the DC-DC boost converter temperature control system.
问题的解决方案  Problem solution
技术解决方案  Technical solution
[0007] 为解决上述第一个技术问题, 本发明的技术方案是: 一种燃料电池汽车的 DC- DC升压转换器控温系统, 包括:  [0007] In order to solve the above first technical problem, the technical solution of the present invention is: A DC-DC boost converter temperature control system for a fuel cell vehicle, comprising:
[0008] 甲醇容器, 其内储存有以甲醇为主的液体; [0008] a methanol container in which a methanol-based liquid is stored;
[0009] 输送泵, 用于将甲醇容器中的甲醇液体通过输送管道泵送至制氢系统;  [0009] a transfer pump for pumping methanol liquid in the methanol container to the hydrogen production system through the delivery pipe;
[0010] DC-DC升压转换器, 用于将燃料电池输出的低压直流电转换为汽车马达所需要 的高压直流电; 所述 DC-DC升压转换器具有甲醇控温器, 所述甲醇液体在输送 泵的泵送过程中, 流经该甲醇控温器, 以控制 DC-DC升压转换器的工作温度; [0011] 制氢系统, 用于甲醇制氢, 制得的氢气供应给燃料电池; [0010] a DC-DC boost converter for converting low-voltage direct current output from a fuel cell into high-voltage direct current required for an automobile motor; the DC-DC boost converter having a methanol temperature controller, wherein the methanol liquid is During the pumping process of the transfer pump, the methanol temperature controller is passed to control the operating temperature of the DC-DC boost converter; [0011] a hydrogen production system for hydrogen production from methanol, and the hydrogen produced is supplied to the fuel cell. ;
[0012] 燃料电池, 用于氢气及空气中的氧气发生电化学反应产生低压直流电, 该低压 直流电经 DC-DC升压转换器转换成高压直流电后, 供应给汽车马达; [0012] a fuel cell for electrochemical reaction of hydrogen and oxygen in the air to generate low-voltage direct current, the low voltage The DC power is converted into high voltage direct current through a DC-DC boost converter and supplied to the automobile motor;
[0013] 以及控制系统, 用于控制所述输送泵、 DC-DC升压转换器、 制氢系统及燃料电 池的工作运转。 And a control system for controlling the operation of the transfer pump, the DC-DC boost converter, the hydrogen production system, and the fuel cell.
[0014] 优选地, 所述 DC-DC升压转换器控温系统还包括三通调节分流阀和三通合流阀 , 所述三通调节分流阀的进液口与输送泵相连通, 所述输送泵泵送的甲醇液体 经三通调节分流阀后分成两路流体, 其中, 第一路流体经 DC-DC升压转换器的 甲醇控温器后进入三通合流阀, 第二路流体直接进入三通合流阀; 两路流体在 三通合流阀中合流后, 输送至制氢系统。 进一步, 所述 DC-DC升压转换器设置 有温度感应器, 该温度感应器与控制系统电性连接。  [0014] Preferably, the DC-DC boost converter temperature control system further includes a three-way regulating diverter valve and a three-way confluence valve, wherein the inlet port of the three-way regulating diverter valve is in communication with the transfer pump, The methanol liquid pumped by the pump is divided into two fluids through the three-way regulating diverter valve, wherein the first fluid passes through the methanol temperature controller of the DC-DC boost converter and enters the three-way confluence valve, and the second fluid directly Enter the three-way confluence valve; the two fluids are combined in the three-way confluence valve and sent to the hydrogen production system. Further, the DC-DC boost converter is provided with a temperature sensor, and the temperature sensor is electrically connected to the control system.
[0015] 优选地, 所述制氢系统包括换热器和重整器, 所述换热器安装于甲醇液体的输 送管道上, 甲醇液体在换热器中, 与重整器输出的高温氢气进行换热, 甲醇液 体温度升高, 氢气温度降低; 所述重整器设有重整室、 加热装置及氢气纯化装 置, 所述加热装置为重整室提供 350-570°C温度的热能; 所述重整室内设有催化 齐 1J, 在重整室内, 发生甲醇和水的重整制氢反应, 制得以二氧化碳和氢气为主 的高温混合气体; 所述重整室与氢气纯化装置通过连接管路连接, 连接管路的 全部或部分设置于重整室内, 能通过重整室内的高温继续加热从重整室输出的 高温混合气体; 所述连接管路作为重整室与氢气纯化装置之间的缓冲, 使得从 重整室输出的高温混合气体的温度与氢气纯化装置的温度相同或接近; 从氢气 纯化装置的产气端得到氢气, 该氢气经换热器后输出至燃料电池。  [0015] Preferably, the hydrogen production system comprises a heat exchanger and a reformer, the heat exchanger is installed on a conveying pipe of a methanol liquid, the methanol liquid is in the heat exchanger, and the high temperature hydrogen gas is outputted from the reformer. Performing heat exchange, the temperature of the methanol liquid is raised, and the temperature of the hydrogen is lowered; the reformer is provided with a reforming chamber, a heating device and a hydrogen purifying device, and the heating device provides heat energy of a temperature of 350-570 ° C for the reforming chamber; The reforming chamber is provided with a catalyst 1J, and in the reforming chamber, a hydrogenation reaction of methanol and water occurs to produce a high-temperature mixed gas mainly composed of carbon dioxide and hydrogen; and the reforming chamber is connected with a hydrogen purifying device. The pipeline connection, all or part of the connecting pipeline is disposed in the reforming chamber, and can continue to heat the high-temperature mixed gas output from the reforming chamber through the high temperature in the reforming chamber; the connecting pipeline serves as a reforming chamber and a hydrogen purifying device The buffering is such that the temperature of the high temperature mixed gas output from the reforming chamber is the same as or close to the temperature of the hydrogen purifying device; hydrogen gas is obtained from the gas producing end of the hydrogen purifying device, After air through the heat exchanger to the output of the fuel cell.
[0016] 优选地, 所述重整器的加热装置为电加热器或者电磁加热器或者氢气燃料腔。  [0016] Preferably, the heating device of the reformer is an electric heater or an electromagnetic heater or a hydrogen fuel chamber.
[0017] 为解决上述第二个技术问题, 本发明的技术方案是: 一种燃料电池汽车的 DC- DC升压转换器控温系统的控温方法, 包括以下步骤:  [0017] In order to solve the above second technical problem, the technical solution of the present invention is: A temperature control method for a DC-DC boost converter temperature control system of a fuel cell vehicle, comprising the following steps:
[0018] (1) 甲醇容器中的甲醇液体在输送泵的泵送作用力下, 流经 DC-DC升压转换 器的甲醇控温器, 甲醇液体在流经甲醇控温器的过程中, 带走 DC-DC升压转换 器中的热量, 并使甲醇液体温度上升;  [0018] (1) The methanol liquid in the methanol container flows through the methanol temperature controller of the DC-DC boost converter under the pumping force of the transfer pump, and the methanol liquid flows through the methanol temperature controller. Take away the heat in the DC-DC boost converter and raise the temperature of the methanol liquid;
[0019] (2) 温度上升后的甲醇液体进入制氢系统, 在制氢系统中, 甲醇液体温度继 续上升, 甲醇和水发生重整制氢反应, 制得氢气, 并供应给燃料电池;  [0019] (2) the methanol liquid after the temperature rise enters the hydrogen production system, in the hydrogen production system, the temperature of the methanol liquid continues to rise, the methanol and water undergo a reforming hydrogen production reaction, and hydrogen is produced and supplied to the fuel cell;
[0020] (3) 在燃料电池内, 氢气及空气中的氧气发生电化学反应产生低压直流电, 该低压直流电经 DC-DC升压转换器转换成高压直流电后, 供应给汽车马达。 [0020] (3) In the fuel cell, hydrogen and oxygen in the air react electrochemically to generate low-voltage direct current, The low-voltage direct current is converted into high-voltage direct current by a DC-DC boost converter and supplied to the automobile motor.
[0021] 优选地, 所述输送泵泵送的甲醇液体经三通调节分流阀后分成两路流体, 其中 , 第一路流体经 DC-DC升压转换器的甲醇控温器后进入三通合流阀, 第二路流 体直接进入三通合流阀; 两路流体在三通合流阀中合流后, 输送至制氢系统; 控制系统根据 DC-DC升压转换器的温度, 通过三通调节分流阀控制流经甲醇控 温器的甲醇液体流量, 当 DC-DC升压转换器温度过高吋, 控制系统控制三通调 节分流阀加大第一路流体的流量, 第二路流体的流量则相应减少; 当 DC-DC升 压转换器温度偏低吋, 控制系统控制三通调节分流阀减少第一路流体的流量, 第二路流体的流量则相应加大。 [0021] Preferably, the methanol liquid pumped by the pump is divided into two channels by a three-way regulating diverter valve, wherein the first channel fluid enters the tee through the methanol temperature controller of the DC-DC boost converter Confluence valve, the second fluid directly enters the three-way confluence valve; the two fluids are combined in the three-way confluence valve and sent to the hydrogen production system; the control system adjusts the diversion through the three-way according to the temperature of the DC-DC boost converter The valve controls the flow of methanol liquid flowing through the methanol temperature controller. When the temperature of the DC-DC boost converter is too high, the control system controls the three-way regulating diverter valve to increase the flow rate of the first fluid, and the flow rate of the second fluid is Corresponding reduction; When the DC-DC boost converter temperature is low, the control system controls the three-way regulating diverter valve to reduce the flow of the first fluid, and the flow of the second fluid is correspondingly increased.
[0022] 优选地, 所述 DC-DC升压转换器设置温度感应器, 该温度感应器实吋将 DC-DC 升压转换器的温度信号反馈给控制系统, 控制系统根据该温度信号, 调节流经 甲醇控温器的甲醇液体流量, 以控制 DC-DC升压转换器的温度处于设定的范围 内。 [0022] Preferably, the DC-DC boost converter is provided with a temperature sensor that feeds back a temperature signal of the DC-DC boost converter to the control system, and the control system adjusts according to the temperature signal. The flow of methanol liquid flowing through the methanol temperature controller to control the temperature of the DC-DC boost converter to be within a set range.
发明的有益效果  Advantageous effects of the invention
有益效果  Beneficial effect
[0023] 本发明的有益效果是: 其一、 本发明的 DC-DC升压转换器采用甲醇控温器散热 , 无需另外设置增压泵和风扇, 占用空间小、 无噪声, 有利于整个燃料电池汽 车的设备布局和降噪; 其二、 DC-DC升压转换器的甲醇控温器巧妙地利用甲醇 液体带走 DC-DC升压转换器产生的热量, 无需另外设置液冷散热风扇, 无需耗 费电能; 其三、 甲醇液体带走 DC-DC升压转换器产生的热量后, 能使甲醇液体 温度提升, 从而使 DC-DC升压转换器产生的热量得到了巧妙的利用; 其五、 又 由于 DC-DC升压转换器产生的热量得到了利用, 从而使 DC-DC升压转换器, 不 会向燃料电池汽车内部排出热量, 保障了燃料电池汽车的工作稳定性。 此外, 在本发明优选方式中, 设置了三通调节分流阀和三通合流阀, 从而使得本发明 的控制系统能根据 DC-DC升压转换器的温度信号, 调节流经甲醇控温器的甲醇 液体流量, 以控制 DC-DC升压转换器的温度处于设定的范围内, 稳定、 可靠。 对附图的简要说明  [0023] The beneficial effects of the present invention are as follows: 1. The DC-DC boost converter of the present invention uses a methanol temperature controller to dissipate heat, and does not need to additionally provide a booster pump and a fan, which occupies small space and is noise-free, and is beneficial to the entire fuel. The battery layout and noise reduction of the battery car; Second, the methanol temperature controller of the DC-DC boost converter skillfully uses the methanol liquid to take away the heat generated by the DC-DC boost converter, without the need to additionally provide a liquid cooling fan. No need to consume electric energy; Third, the methanol liquid takes away the heat generated by the DC-DC boost converter, which can raise the temperature of the methanol liquid, so that the heat generated by the DC-DC boost converter is skillfully utilized; Moreover, the heat generated by the DC-DC boost converter is utilized, so that the DC-DC boost converter does not discharge heat to the interior of the fuel cell vehicle, thereby ensuring the operational stability of the fuel cell vehicle. In addition, in a preferred mode of the present invention, a three-way regulating diverter valve and a three-way confluence valve are provided, so that the control system of the present invention can adjust the flow of the methanol temperature controller according to the temperature signal of the DC-DC boost converter. The methanol liquid flow rate is controlled to be stable and reliable by controlling the temperature of the DC-DC boost converter within a set range. Brief description of the drawing
附图说明 [0024] 图 1为本发明的整体结构方框图。 DRAWINGS 1 is a block diagram showing the overall structure of the present invention.
[0025] 图 2为本发明一优选方式的整体结构方框图。  2 is a block diagram showing the overall structure of a preferred embodiment of the present invention.
本发明的实施方式 Embodiments of the invention
[0026] 下面结合附图对本发明的结构原理和工作原理作进一步详细说明。 The structural principle and working principle of the present invention will be further described in detail below with reference to the accompanying drawings.
[0027] 如图 1所述, 本发明为一种燃料电池汽车的 DC-DC升压转换器控温系统, 包括 [0027] As shown in FIG. 1, the present invention is a DC-DC boost converter temperature control system for a fuel cell vehicle, including
[0028] 甲醇容器 1, 其内储存有以甲醇为主的液体, 优选为甲醇水溶液; [0028] The methanol container 1 stores therein a methanol-based liquid, preferably an aqueous methanol solution;
[0029] 输送泵 2, 用于将甲醇容器 1中的甲醇液体通过输送管道泵送至制氢系统; [0030] DC-DC升压转换器 3, 用于将燃料电池 5输出的低压直流电转换为汽车马达 7所 需要的高压直流电, 该低压直流电通常为 15〜35V的直流电, 该高压直流电通常 为 200〜750V的直流电; 所述 DC-DC升压转换器 3具有甲醇控温器 31, 所述甲醇 液体在输送泵 2的泵送过程中, 流经该甲醇控温器 31, 以控制 DC-DC升压转换器 3的工作温度; [0029] a transfer pump 2 for pumping the methanol liquid in the methanol container 1 to the hydrogen production system through the delivery pipe; [0030] a DC-DC boost converter 3 for converting the low voltage direct current output of the fuel cell 5 The high-voltage direct current required for the automobile motor 7, the low-voltage direct current is usually 15~35V direct current, the high-voltage direct current is usually 200~750V direct current; the DC-DC boost converter 3 has a methanol temperature controller 31, The methanol liquid flows through the methanol temperature controller 31 during the pumping process of the transfer pump 2 to control the operating temperature of the DC-DC boost converter 3;
[0031] 制氢系统, 用于甲醇制氢, 制得的氢气供应给燃料电池 6;  [0031] a hydrogen production system for hydrogen production from methanol, the hydrogen produced is supplied to the fuel cell 6;
[0032] 燃料电池 6, 用于氢气及空气中的氧气发生电化学反应产生低压直流电, 在燃 料电池的阳极: 2H 2→4H ++4e -, H 2分裂成两个质子和两个电子, 质子穿过质子 交换膜 (PEM) , 电子通过阳极板, 通过外部负载, 并进入阴极双极板, 在燃 料电池的阴极: 0 2+4e -+4H +→2H 20, 质子、 电子和 0 2重新结合以形成11 20; 该低压直流电经 DC-DC升压转换器 3转换成高压直流电后, 供应给汽车马达 7; [0032] The fuel cell 6, for the electrochemical reaction of hydrogen and oxygen in the air to generate low-voltage direct current, at the anode of the fuel cell: 2H 2 → 4H ++ 4e -, H 2 split into two protons and two electrons, Protons pass through the proton exchange membrane (PEM), electrons pass through the anode plate, pass through the external load, and enter the cathode bipolar plate at the cathode of the fuel cell: 0 2 +4e -+4H +→2H 2 0, protons, electrons and 0 2 recombined to form 11 2 0; the low voltage direct current is converted into high voltage direct current by the DC-DC boost converter 3, and then supplied to the automobile motor 7;
[0033] 以及控制系统 (图中未示出) , 用于控制所述输送泵 2、 DC-DC升压转换器 3、 制氢系统及燃料电池 6的工作运转。  And a control system (not shown) for controlling the operation of the transfer pump 2, the DC-DC boost converter 3, the hydrogen production system, and the fuel cell 6.
[0034] 如图 2所示, 所述 DC-DC升压转换器控温系统还包括三通调节分流阀 8和三通合 流阀 9, 所述三通调节分流阀 8的进液口与输送泵 2相连通, 所述输送泵 2泵送的 甲醇液体经三通调节分流阀 8后分成两路流体, 其中, 第一路流体经 DC-DC升压 转换器 3的甲醇控温器 31后进入三通合流阀 9, 第二路流体直接进入三通合流阀 9 ; 两路流体在三通合流阀 9中合流后, 输送至制氢系统, 通过对三通调节分流阀 8的控制, 双面使 DC-DC升压转换器的温度处于设定的范围内, 稳定、 可靠。 进 一步, 所述 DC-DC升压转换器 3设置有温度感应器 (图中未示出), 该温度感应器 与控制系统电性连接, 这样能使控制系统实吋监控 DC-DC升压转换器 3的温度。 [0034] As shown in FIG. 2, the DC-DC boost converter temperature control system further includes a three-way regulating diverter valve 8 and a three-way confluence valve 9, the three-way regulating diverter valve 8 inlet and delivery The pump 2 is in communication, and the methanol liquid pumped by the pump 2 is divided into two channels by the three-way regulating diverter valve 8, wherein the first channel fluid passes through the methanol temperature controller 31 of the DC-DC boost converter 3. Entering the three-way confluence valve 9, the second fluid directly enters the three-way confluence valve 9; the two fluids are merged in the three-way confluence valve 9, and then sent to the hydrogen production system, through the control of the three-way regulating diverter valve 8, The surface makes the temperature of the DC-DC boost converter within the set range, stable and reliable. Enter In one step, the DC-DC boost converter 3 is provided with a temperature sensor (not shown), and the temperature sensor is electrically connected to the control system, so that the control system can monitor the DC-DC boost conversion. The temperature of the device 3.
[0035] 在上述技术方案中, 所述制氢系统包括换热器 5和重整器 4, 所述换热器 5安装 于甲醇液体的输送管道上, 甲醇液体在换热器 5中, 与重整器 4输出的高温氢气 进行换热, 甲醇液体温度升高, 氢气温度降低; 所述重整器 4设有重整室 41、 加 热装置 42及氢气纯化装置 43, 所述加热装置 42为重整室 41提供 350-570°C温度的 热能; 所述重整室 41内设有催化剂, 在催化剂的作用下, 发生甲醇裂解反应和 一氧化碳的变换反应, 生成氢气和二氧化碳, 这是一个多组份、 多反应的气固 催化反应系统, 反应方程为: (l)CH 3OH→CO+2H 2、 (2)H 20+CO→CO 2+H 2 、 (3)CH 3OH+H 20→C0 2+3H 2, 制得以二氧化碳和氢气为主的高温混合气体; 所述重整室 41与氢气纯化装置 43通过连接管路连接, 连接管路的全部或部分设 置于重整室 41内, 能通过重整室 41内的高温继续加热从重整室 41输出的高温混 合气体; 所述连接管路作为重整室 41与氢气纯化装置 43之间的缓冲, 使得从重 整室 41输出的高温混合气体的温度与氢气纯化装置 43的温度相同或接近; 从氢 气纯化装置 43的产气端得到氢气, 该氢气经换热器 5后输出至燃料电池 6。 [0035] In the above technical solution, the hydrogen production system includes a heat exchanger 5 and a reformer 4, the heat exchanger 5 is installed on a conveying pipe of a methanol liquid, and the methanol liquid is in the heat exchanger 5, The high-temperature hydrogen outputted by the reformer 4 performs heat exchange, the temperature of the methanol liquid rises, and the temperature of the hydrogen gas decreases. The reformer 4 is provided with a reforming chamber 41, a heating device 42, and a hydrogen purifying device 43, wherein the heating device 42 is The reforming chamber 41 provides thermal energy at a temperature of 350-570 ° C; the reforming chamber 41 is provided with a catalyst, and under the action of the catalyst, a methanol cracking reaction and a carbon monoxide shift reaction are generated to generate hydrogen gas and carbon dioxide, which is more than one. Component, multi-reaction gas-solid catalytic reaction system, the reaction equation is: (l) CH 3 OH → CO + 2H 2 , (2) H 2 0 + CO → CO 2 + H 2 , (3) CH 3 OH + H 2 0→C0 2 +3H 2 , a high-temperature mixed gas mainly composed of carbon dioxide and hydrogen; the reforming chamber 41 and the hydrogen purifying device 43 are connected by a connecting pipe, and all or part of the connecting pipe is set in the reforming In the chamber 41, the heating can be continued from the reforming chamber 41 by the high temperature in the reforming chamber 41. a high-temperature mixed gas; the connecting line acts as a buffer between the reforming chamber 41 and the hydrogen purifying device 43, so that the temperature of the high-temperature mixed gas output from the reforming chamber 41 is the same as or close to the temperature of the hydrogen purifying device 43; Hydrogen is obtained from the gas producing end of the hydrogen purifying unit 43, and the hydrogen is supplied to the fuel cell 6 via the heat exchanger 5.
[0036] 在上述技术方案中, 所述重整器 4的加热装置 42可采用电加热器或者电磁加热 器或者氢气燃料腔, 优选于采用电磁加热器, 具体技术内容参照中国专利申请 2 01510754381.7。  In the above technical solution, the heating device 42 of the reformer 4 may be an electric heater or an electromagnetic heater or a hydrogen fuel chamber, preferably an electromagnetic heater. For details, refer to Chinese Patent Application No. 2,151,075,438, 1.7.
[0037] 上述燃料电池汽车的 DC-DC升压转换器控温系统的控温方法, 包括以下步骤: [0038] (1) 甲醇容器中的甲醇液体在输送泵的泵送作用力下, 流经 DC-DC升压转换 器的甲醇控温器, 甲醇液体在流经甲醇控温器的过程中, 带走 DC-DC升压转换 器中的热量, 并使甲醇液体温度上升;  [0037] The temperature control method of the DC-DC boost converter temperature control system of the fuel cell automobile includes the following steps: [0038] (1) The methanol liquid in the methanol container flows under the pumping force of the transfer pump Through the methanol temperature controller of the DC-DC boost converter, the methanol liquid takes away the heat in the DC-DC boost converter during the flow through the methanol temperature controller, and raises the temperature of the methanol liquid;
[0039] (2) 温度上升后的甲醇液体进入制氢系统, 在制氢系统中, 甲醇液体温度继 续上升, 甲醇和水发生重整制氢反应, 制得氢气, 并供应给燃料电池; [0039] (2) the methanol liquid after the temperature rise enters the hydrogen production system, in the hydrogen production system, the temperature of the methanol liquid continues to rise, the methanol and water undergo a reforming hydrogen production reaction, and hydrogen is produced and supplied to the fuel cell;
[0040] (3) 在燃料电池内, 氢气及空气中的氧气发生电化学反应产生低压直流电, 该低压直流电经 DC-DC升压转换器转换成高压直流电后, 供应给汽车马达。 [0040] (3) In the fuel cell, hydrogen gas and oxygen in the air electrochemically react to generate low-voltage direct current, which is converted into high-voltage direct current by a DC-DC boost converter and supplied to the automobile motor.
[0041] 作为对本发明的优选方式, 所述输送泵泵送的甲醇液体经三通调节分流阀后分 成两路流体, 其中, 第一路流体经 DC-DC升压转换器的甲醇控温器后进入三通 合流阀, 第二路流体直接进入三通合流阀; 两路流体在三通合流阀中合流后, 输送至制氢系统; 控制系统根据 DC-DC升压转换器的温度, 通过三通调节分流 阀控制流经甲醇控温器的甲醇液体流量, 当 DC-DC升压转换器温度过高吋, 控 制系统控制三通调节分流阀加大第一路流体的流量, 第二路流体的流量则相应 减少; 当 DC-DC升压转换器温度偏低吋, 控制系统控制三通调节分流阀减少第 一路流体的流量, 第二路流体的流量则相应加大。 [0041] As a preferred mode of the present invention, the methanol liquid pumped by the transfer pump is divided into two channels by a three-way regulating diverter valve, wherein the first path fluid passes through the methanol temperature controller of the DC-DC boost converter. After entering the three links Confluence valve, the second fluid directly enters the three-way confluence valve; the two fluids are combined in the three-way confluence valve and sent to the hydrogen production system; the control system adjusts the diversion through the three-way according to the temperature of the DC-DC boost converter The valve controls the flow of methanol liquid flowing through the methanol temperature controller. When the temperature of the DC-DC boost converter is too high, the control system controls the three-way regulating diverter valve to increase the flow rate of the first fluid, and the flow rate of the second fluid is Corresponding reduction; When the DC-DC boost converter temperature is low, the control system controls the three-way regulating diverter valve to reduce the flow of the first fluid, and the flow of the second fluid is correspondingly increased.
[0042] 进一步地, 所述 DC-DC升压转换器设置温度感应器, 该温度感应器实吋将 DC- DC升压转换器的温度信号反馈给控制系统, 控制系统根据该温度信号, 调节流 经甲醇控温器的甲醇液体流量, 以控制 DC-DC升压转换器的温度处于设定的范 围内。 [0042] Further, the DC-DC boost converter is provided with a temperature sensor, and the temperature sensor actually feeds back a temperature signal of the DC-DC boost converter to the control system, and the control system adjusts according to the temperature signal. The flow of methanol liquid flowing through the methanol temperature controller to control the temperature of the DC-DC boost converter to be within a set range.
[0043] 以上所述, 仅是本发明较佳实施方式, 凡是依据本发明的技术方案对以上的实 施方式所作的任何细微修改、 等同变化与修饰, 均属于本发明技术方案的范围 内。  The above is only the preferred embodiment of the present invention, and any minor modifications, equivalent changes and modifications to the above embodiments in accordance with the technical solutions of the present invention are within the scope of the technical solutions of the present invention.
工业实用性  Industrial applicability
[0044] 本发明为一种燃料电池汽车的 DC-DC升压转换器控温系统及方法, 该 DC-DC升 压转换器控温系统噪音低、 散热效果好、 耗能低, 占用空间小, 并且燃料电池 汽车能够有效利用 DC-DC升压转换器所产生的热量, 不会因为 DC-DC升压转换 器热量的排出而影响燃料电池汽车的其他电子电路工作运转。 因此, 具有工业 实用性。  [0044] The present invention is a fuel cell vehicle DC-DC boost converter temperature control system and method, the DC-DC boost converter temperature control system has low noise, good heat dissipation effect, low energy consumption, and small space occupation And the fuel cell vehicle can effectively utilize the heat generated by the DC-DC boost converter, and does not affect the operation of other electronic circuits of the fuel cell vehicle due to the discharge of the heat of the DC-DC boost converter. Therefore, it has industrial applicability.

Claims

权利要求书 Claim
燃料电池汽车的 DC-DC升压转换器控温系统, 其特征在于, 包括: 甲醇容器, 其内储存有以甲醇为主的液体; A DC-DC boost converter temperature control system for a fuel cell vehicle, comprising: a methanol container in which a methanol-based liquid is stored;
输送泵, 用于将甲醇容器中的甲醇液体通过输送管道泵送至制氢系统 a transfer pump for pumping methanol liquid in a methanol container to a hydrogen production system through a transfer line
DC-DC升压转换器, 用于将燃料电池输出的低压直流电转换为汽车 马达所需要的高压直流电; 所述 DC-DC升压转换器具有甲醇控温器 , 所述甲醇液体在输送泵的泵送过程中, 流经该甲醇控温器, 以控制 DC-DC升压转换器的工作温度; a DC-DC boost converter for converting low-voltage direct current output from a fuel cell into high-voltage direct current required for an automobile motor; the DC-DC boost converter having a methanol temperature controller, the methanol liquid being in a transfer pump During the pumping process, flowing through the methanol temperature controller to control the operating temperature of the DC-DC boost converter;
制氢系统, 用于甲醇制氢, 制得的氢气供应给燃料电池; a hydrogen production system for hydrogen production from methanol, and the produced hydrogen is supplied to the fuel cell;
燃料电池, 用于氢气及空气中的氧气发生电化学反应产生低压直流电 , 该低压直流电经 DC-DC升压转换器转换成高压直流电后, 供应给 汽车马达; A fuel cell for electrochemically reacting oxygen in hydrogen and air to generate low-voltage direct current, which is converted into high-voltage direct current by a DC-DC boost converter and supplied to an automobile motor;
以及控制系统, 用于控制所述输送泵、 DC-DC升压转换器、 制氢系 统及燃料电池的工作运转。 And a control system for controlling the operation of the transfer pump, the DC-DC boost converter, the hydrogen production system, and the fuel cell.
根据权利要求 1所述的 DC-DC升压转换器控温系统, 其特征在于: 所 述 DC-DC升压转换器控温系统还包括三通调节分流阀和三通合流阀 , 所述三通调节分流阀的进液口与输送泵相连通, 所述输送泵泵送的 甲醇液体经三通调节分流阀后分成两路流体, 其中, 第一路流体经 D C-DC升压转换器的甲醇控温器后进入三通合流阀, 第二路流体直接 进入三通合流阀; 两路流体在三通合流阀中合流后, 输送至制氢系统 根据权利要求 2所述的 DC-DC升压转换器控温系统, 其特征在于: 所 述 DC-DC升压转换器设置有温度感应器, 该温度感应器与控制系统 电性连接。 The DC-DC boost converter temperature control system according to claim 1, wherein: said DC-DC boost converter temperature control system further comprises a three-way regulating diverter valve and a three-way confluence valve, said three The inlet port of the regulating diverter valve is in communication with the transfer pump, and the methanol liquid pumped by the transfer pump is divided into two channels by a three-way regulating diverter valve, wherein the first channel fluid passes through the D C-DC boost converter After the methanol temperature controller enters the three-way confluence valve, the second fluid directly enters the three-way confluence valve; after the two fluids are merged in the three-way confluence valve, the two-way confluence valve is delivered to the hydrogen production system according to claim 2 The boost converter temperature control system is characterized in that: the DC-DC boost converter is provided with a temperature sensor, and the temperature sensor is electrically connected to the control system.
根据权利要求 1所述的 DC-DC升压转换器控温系统, 其特征在于: 所 述制氢系统包括换热器和重整器, 所述换热器安装于甲醇液体的输送 管道上, 甲醇液体在换热器中, 与重整器输出的高温氢气进行换热, 甲醇液体温度升高, 氢气温度降低; 所述重整器设有重整室、 加热装 置及氢气纯化装置, 所述加热装置为重整室提供 350-570°C温度的热 育 ; 所述重整室内设有催化剂, 在重整室内, 发生甲醇和水的重整制 氢反应, 制得以二氧化碳和氢气为主的高温混合气体; 所述重整室与 氢气纯化装置通过连接管路连接, 连接管路的全部或部分设置于重整 室内, 能通过重整室内的高温继续加热从重整室输出的高温混合气体 ; 所述连接管路作为重整室与氢气纯化装置之间的缓冲, 使得从重整 室输出的高温混合气体的温度与氢气纯化装置的温度相同或接近; 从 氢气纯化装置的产气端得到氢气, 该氢气经换热器后输出至燃料电池 The DC-DC boost converter temperature control system according to claim 1, wherein: the hydrogen production system comprises a heat exchanger and a reformer, and the heat exchanger is installed on a conveying pipe of a methanol liquid, The methanol liquid is in the heat exchanger and exchanges heat with the high temperature hydrogen output from the reformer. The temperature of the methanol liquid is increased, and the temperature of the hydrogen is lowered; the reformer is provided with a reforming chamber, a heating device and a hydrogen purifying device, and the heating device provides a temperature of 350-570 ° C for the reforming chamber; The whole chamber is provided with a catalyst, and in the reforming chamber, a hydrogenation reaction of methanol and water occurs to produce a high-temperature mixed gas mainly composed of carbon dioxide and hydrogen; and the reforming chamber and the hydrogen purifying device are connected through a connecting pipe, and are connected. All or part of the pipeline is disposed in the reforming chamber, and the high-temperature mixed gas output from the reforming chamber can be continuously heated by the high temperature in the reforming chamber; the connecting pipeline acts as a buffer between the reforming chamber and the hydrogen purifying device, so that The temperature of the high temperature mixed gas output from the reforming chamber is the same as or close to the temperature of the hydrogen purifying device; hydrogen gas is obtained from the gas producing end of the hydrogen purifying device, and the hydrogen gas is output to the fuel cell through the heat exchanger
[权利要求 5] 根据权利要求 4所述的 DC-DC升压转换器控温系统, 其特征在于: 所 述重整器的加热装置为电加热器或者电磁加热器或者氢气燃料腔。 [Claim 5] The DC-DC boost converter temperature control system according to claim 4, wherein the heating device of the reformer is an electric heater or an electromagnetic heater or a hydrogen fuel chamber.
[权利要求 6] 权利要求 1-5中任意一项所述燃料电池汽车的 DC-DC升压转换器控温 系统的控温方法, 其特征在于, 包括以下步骤:  [Claim 6] The temperature control method of the DC-DC boost converter temperature control system of the fuel cell vehicle according to any one of claims 1 to 5, characterized in that it comprises the following steps:
(1) 甲醇容器中的甲醇液体在输送泵的泵送作用力下, 流经 DC-DC 升压转换器的甲醇控温器, 甲醇液体在流经甲醇控温器的过程中, 带 走 DC-DC升压转换器中的热量, 并使甲醇液体温度上升;  (1) The methanol liquid in the methanol container flows through the methanol temperature controller of the DC-DC boost converter under the pumping force of the transfer pump, and the methanol liquid takes away the DC during the process of flowing through the methanol temperature controller. - heat in the DC boost converter and raise the temperature of the methanol liquid;
(2) 温度上升后的甲醇液体进入制氢系统, 在制氢系统中, 甲醇液 体温度继续上升, 甲醇和水发生重整制氢反应, 制得氢气, 并供应给 燃料电池;  (2) The methanol liquid after the temperature rise enters the hydrogen production system. In the hydrogen production system, the temperature of the methanol liquid continues to rise, and the methanol and water undergo a reforming hydrogen production reaction to produce hydrogen gas, which is supplied to the fuel cell;
(3) 在燃料电池内, 氢气及空气中的氧气发生电化学反应产生低压 直流电, 该低压直流电经 DC-DC升压转换器转换成高压直流电后, 供应给汽车马达。  (3) In the fuel cell, hydrogen gas and oxygen in the air react electrochemically to generate low-voltage direct current, which is converted into high-voltage direct current by a DC-DC boost converter and supplied to the automobile motor.
[权利要求 7] 根据权利要求 6所述的 DC-DC升压转换器控温系统的控温方法, 其特 征在于: 所述输送泵泵送的甲醇液体经三通调节分流阀后分成两路流 体, 其中, 第一路流体经 DC-DC升压转换器的甲醇控温器后进入三 通合流阀, 第二路流体直接进入三通合流阀; 两路流体在三通合流阀 中合流后, 输送至制氢系统; 控制系统根据 DC-DC升压转换器的温 度, 通过三通调节分流阀控制流经甲醇控温器的甲醇液体流量, 当 D C-DC升压转换器温度过高吋, 控制系统控制三通调节分流阀加大第 一路流体的流量, 第二路流体的流量则相应减少; 当 DC-DC升压转 换器温度偏低吋, 控制系统控制三通调节分流阀减少第一路流体的流 量, 第二路流体的流量则相应加大。 [Claim 7] The temperature control method of the DC-DC boost converter temperature control system according to claim 6, wherein: the methanol liquid pumped by the transfer pump is divided into two paths after adjusting the diverter valve through the three-way a fluid, wherein the first fluid passes through the methanol temperature controller of the DC-DC boost converter and enters the three-way confluence valve, and the second fluid directly enters the three-way confluence valve; after the two fluids merge in the three-way confluence valve , to the hydrogen production system; the control system is based on the temperature of the DC-DC boost converter Degree, through the three-way regulating diverter valve to control the flow of methanol liquid flowing through the methanol temperature controller, when the temperature of the D C-DC boost converter is too high, the control system controls the three-way regulating diverter valve to increase the flow rate of the first fluid The flow rate of the second fluid is correspondingly reduced; when the temperature of the DC-DC boost converter is low, the control system controls the three-way regulating diverter valve to reduce the flow of the first fluid, and the flow of the second fluid is correspondingly increased. .
[权利要求 8] 根据权利要求 7所述的 DC-DC升压转换器控温系统的控温方法, 其特 征在于: 所述 DC-DC升压转换器设置温度感应器, 该温度感应器实 吋将 DC-DC升压转换器的温度信号反馈给控制系统, 控制系统根据 该温度信号, 调节流经甲醇控温器的甲醇液体流量, 以控制 DC-DC 升压转换器的温度处于设定的范围内。 [Claim 8] The temperature control method of the DC-DC boost converter temperature control system according to claim 7, wherein: the DC-DC boost converter is provided with a temperature sensor, and the temperature sensor is反馈 The temperature signal of the DC-DC boost converter is fed back to the control system, and the control system adjusts the flow rate of the methanol liquid flowing through the methanol temperature controller according to the temperature signal to control the temperature of the DC-DC boost converter to be set. In the range.
PCT/CN2016/085894 2016-01-06 2016-06-15 Temperature control system and method for dc-dc boost converter of fuel cell automobile WO2017117918A1 (en)

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