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CN106711477A - Cooling circulation process for fuel cell - Google Patents

Cooling circulation process for fuel cell Download PDF

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Publication number
CN106711477A
CN106711477A CN201610835222.4A CN201610835222A CN106711477A CN 106711477 A CN106711477 A CN 106711477A CN 201610835222 A CN201610835222 A CN 201610835222A CN 106711477 A CN106711477 A CN 106711477A
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fuel cell
cooling
circulation
temperature
circulation loop
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牛萌
刘锋
肖宇
赵鹏程
杜兆龙
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Global Energy Interconnection Research Institute Co Ltd
State Grid Corp of China SGCC
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Global Energy Interconnection Research Institute Co Ltd
State Grid Corp of China SGCC
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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
    • 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
    • H01M8/04007Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids related to heat exchange
    • H01M8/04067Heat exchange or temperature measuring elements, thermal insulation, e.g. heat pipes, heat pumps, fins
    • H01M8/04074Heat exchange unit structures specially adapted for fuel cell
    • 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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  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Fuel Cell (AREA)

Abstract

本发明公开一种用于燃料电池的冷却循环工艺,属于燃料电池工程设计技术领域。本发明用于燃料电池的冷却循环工艺,使用包括并联设置的第一循环回路和第二循环回路,所述第一循环回路上设置有热源液体冷却装置;所述第二循环回路上设置有换热装置。本发明的用于燃料电池的冷却循环工艺有利于将燃料电池的热能回收利用,能量转化效率高。

The invention discloses a cooling cycle process for fuel cells, which belongs to the technical field of fuel cell engineering design. The present invention is used for the cooling circulation process of fuel cells, using a first circulation loop and a second circulation loop arranged in parallel, the first circulation loop is provided with a heat source liquid cooling device; the second circulation loop is provided with a heat exchanger heat device. The cooling circulation process for the fuel cell of the present invention is beneficial to recycle the heat energy of the fuel cell, and has high energy conversion efficiency.

Description

一种用于燃料电池的冷却循环工艺A cooling cycle process for fuel cells

技术领域technical field

本发明属于燃料电池工程设计技术领域,具体涉及一种用于燃料电池的冷却循环工艺。The invention belongs to the technical field of fuel cell engineering design, and in particular relates to a cooling cycle process for fuel cells.

背景技术Background technique

随着工业社会的进一步发展,环境问题日益突出,环境友好的氢储能技术得到了越来越多的关注。氢储能技术包括氢气的制取、存储、输送及使用,其产业链最关键一环—燃料电池技术,而燃料电池技术在全世界科学技术人员的攻关下,已经进入产业化的初期。With the further development of industrial society, environmental problems have become increasingly prominent, and environmentally friendly hydrogen energy storage technology has received more and more attention. Hydrogen energy storage technology includes the production, storage, transportation and use of hydrogen. The most critical link in its industrial chain is fuel cell technology. Fuel cell technology has entered the initial stage of industrialization under the research of scientific and technical personnel all over the world.

传统的燃料电池模块仅包括燃料电池电堆、冷却介质传输单元、氢气传输单元、空气传输单元、燃料电池电能控制单元,不具有电堆热能回收单元,不利于将燃料电池的热能回收利用,能量转化效率较低。The traditional fuel cell module only includes the fuel cell stack, the cooling medium transmission unit, the hydrogen transmission unit, the air transmission unit, and the fuel cell power control unit. The conversion efficiency is low.

本领域技术人员一直致力于寻求一种具有电堆热能回收单元从而可将燃料电池的热能回收利用进而提高能量转化效率的工艺。为此,中国专利文献CN 101587962A公开了质子交换膜燃料电池冷却系统,该系统包括传感机构、控制模块、执行机构和冷却机构,其中传感机构的输出端与控制模块的输入端相连接以传输传感信号,控制模块的输出端执行机构的输入端相连接,执行机构的输出端与冷却机构的输入端相连接,冷却机构的输出端与传感机构的输入端相连接。Those skilled in the art have been devoting themselves to finding a process that has a stack heat recovery unit so as to recycle the heat energy of the fuel cell and improve the energy conversion efficiency. For this reason, Chinese patent document CN 101587962A discloses a proton exchange membrane fuel cell cooling system, which system includes a sensing mechanism, a control module, an actuator and a cooling mechanism, wherein the output end of the sensing mechanism is connected with the input end of the control module to Transmitting sensing signals, the output end of the control module is connected to the input end of the actuator, the output end of the actuator is connected to the input end of the cooling mechanism, and the output end of the cooling mechanism is connected to the input end of the sensing mechanism.

该系统通过温度传感器的设置能够将冷却液入口端和出口端的温度数值实时输送至控制模块,控制模块根据实时数据判断选择冷却路线,并通过执行机构控制三通阀的开启方向,从而在一定程度上实现了对温度一级误差波动的控制,该系统通过对温度误差波动的控制部分实现了对燃料电池能量转化效率的提高,但其仅从燃料电池温度控制角度分析而不能根据燃料电池的出口冷却液的温度分级选择冷却循环回路进行能量回收,能量转化效率还不甚理想。The system can transmit the temperature values of the inlet and outlet ports of the coolant to the control module in real time through the setting of the temperature sensor. The control module judges and selects the cooling route according to the real-time data, and controls the opening direction of the three-way valve through the actuator. The system realizes the control of the first-level error fluctuation of the temperature, and the system partially realizes the improvement of the energy conversion efficiency of the fuel cell through the control of the temperature error fluctuation, but it is only analyzed from the perspective of fuel cell temperature control and cannot be analyzed according to the outlet The temperature classification of the cooling liquid selects the cooling circulation loop for energy recovery, and the energy conversion efficiency is not ideal.

发明内容Contents of the invention

为此,本发明针对现有技术的燃料电池模块不能根据燃料电池的出口冷却液的温度分级选择冷却循环回路能量转化效率还不甚理想的技术缺陷,从而提供一种用于燃料电池的冷却循环工艺。For this reason, the present invention aims at the technical defect that the fuel cell module of the prior art cannot be selected according to the temperature classification of the outlet coolant of the fuel cell, and the energy conversion efficiency of the cooling cycle loop is not ideal, thereby providing a cooling cycle for the fuel cell craft.

为解决上述技术问题,本发明采用的技术方案如下:In order to solve the problems of the technologies described above, the technical scheme adopted in the present invention is as follows:

一种用于燃料电池的冷却循环工艺,使用A cooling cycle process for fuel cells, using

包括并联设置的第一循环回路和第二循环回路,所述第一循环回路上设置有热源液体冷却装置;所述第二循环回路上设置有换热装置。It includes a first circulation loop and a second circulation loop arranged in parallel, a heat source liquid cooling device is arranged on the first circulation loop; a heat exchange device is arranged on the second circulation loop.

按如下步骤进行:Proceed as follows:

(1)使燃料电池出口的热源液体经第二循环泵通入所述冷却循环回路;(1) Make the heat source liquid at the outlet of the fuel cell pass into the cooling circulation loop through the second circulation pump;

(2)使所述冷却循环回路输出的热源液体流经第二储液箱,并进一步的流入燃料电池。(2) Make the heat source liquid output by the cooling circulation loop flow through the second liquid storage tank, and further flow into the fuel cell.

所述第二循环回路上还设置有散热装置。A cooling device is also provided on the second circulation loop.

还包括,Also includes,

(1)设置第一温度阈值M1,(1) Setting the first temperature threshold M1,

(2)当流出燃料电池的冷却液温度小于M1时,所述冷却液经第一循环回路返回所述燃料电池;(2) When the temperature of the coolant flowing out of the fuel cell is lower than M1, the coolant returns to the fuel cell through the first circulation loop;

(3)当流出燃料电池的冷却液温度大于M1时,所述冷却液经第二循环回路返回所述燃料电池。(3) When the temperature of the coolant flowing out of the fuel cell is greater than M1, the coolant returns to the fuel cell through the second circulation loop.

还设置有第二温度阈值M2,其中M1小于M2;A second temperature threshold M2 is also set, wherein M1 is smaller than M2;

当流出燃料电池的冷却液温度在M1和M2之间时,所述冷却液经所述换热装置冷却处理后返回燃料电池;When the temperature of the coolant flowing out of the fuel cell is between M1 and M2, the coolant is cooled by the heat exchange device and then returned to the fuel cell;

当流出燃料电池的冷却液温度大于M2时,所述冷却液经所述换热装置和所述散热装置冷却处理后返回燃料电池。When the temperature of the cooling liquid flowing out of the fuel cell is greater than M2, the cooling liquid returns to the fuel cell after being cooled by the heat exchange device and the heat dissipation device.

还包括回路选择装置,用于控制流出所述燃料电池的冷却液进入第一循环回路或第二循环回路。A circuit selection device is also included for controlling the coolant flowing out of the fuel cell to enter the first circulation loop or the second circulation loop.

所述第二循环回路上还设有用于接收所述换热装置热量的第一储液箱。The second circulation loop is also provided with a first liquid storage tank for receiving heat from the heat exchange device.

所述换热装置与所述第一储液箱之间设有第一循环泵。A first circulation pump is provided between the heat exchange device and the first liquid storage tank.

所述换热装置为板式换热器,所述换热器内设有热源液体通道,所述热源液体通道的外围布置有冷却循环液通道,以使冷却循环液通过第一循环泵流入所述第一热储液箱。The heat exchange device is a plate heat exchanger, and a heat source liquid channel is arranged in the heat exchanger, and a cooling circulating liquid channel is arranged on the periphery of the heat source liquid channel, so that the cooling circulating liquid flows into the First heat reservoir.

还包括与燃料电池相连的第二储液箱;A second liquid storage tank connected to the fuel cell is also included;

所述第一循环回路和所述第二循环回路在第二储液箱的入口处汇合;the first circulation loop and the second circulation loop join at the inlet of the second liquid storage tank;

所述回路选择装置通过第二循环泵与燃料电池相连。The circuit selection device is connected with the fuel cell through the second circulation pump.

所述回路选择装置为节温器,所述散热装置为散热器。The circuit selection device is a thermostat, and the heat dissipation device is a radiator.

所述燃料电池热源液体出口处,所述第一储液箱内以及燃料电池热源液体入口处,分别对应设有第一温度传感器,第二温度传感器,第三温度传感器,所述第一温度传感器内设有温度检测装置和信号传输装置用于检测出口温度并传输给第二循环泵、节温器、换热器和散热器。The fuel cell heat source liquid outlet, the first liquid storage tank and the fuel cell heat source liquid inlet are respectively provided with a first temperature sensor, a second temperature sensor, a third temperature sensor, and the first temperature sensor A temperature detection device and a signal transmission device are installed inside to detect the outlet temperature and transmit it to the second circulation pump, thermostat, heat exchanger and radiator.

所述燃料电池选自质子交换膜燃料电池、直接甲醇燃料电池、磷酸燃料电池、熔融碳酸盐燃料电池或高温固体氧化物燃料电池。The fuel cell is selected from proton exchange membrane fuel cell, direct methanol fuel cell, phosphoric acid fuel cell, molten carbonate fuel cell or high temperature solid oxide fuel cell.

本发明中的燃料电池包括但不限于质子交换膜燃料电池、直接甲醇燃料电池、磷酸燃料电池、熔融碳酸盐燃料电池或高温固体氧化物燃料电池的一种或多种的组合。The fuel cell in the present invention includes but not limited to one or more combination of proton exchange membrane fuel cell, direct methanol fuel cell, phosphoric acid fuel cell, molten carbonate fuel cell or high temperature solid oxide fuel cell.

本发明与现有技术相比具有如下优点:Compared with the prior art, the present invention has the following advantages:

1、本发明提供的用于燃料电池的冷却循环工艺采用包括第一循环回路和第二循环回路,所述第一循环回路具有热源液体冷却装置用以冷却较低温度的热源液体,所述第二循环回路具有换热装置用以冷却稍高温度的热源液体。1. The cooling circulation process for fuel cells provided by the present invention includes a first circulation loop and a second circulation loop. The first circulation loop has a heat source liquid cooling device for cooling a lower temperature heat source liquid. The second circulation loop The secondary circulation loop has a heat exchange device to cool the heat source liquid with a slightly higher temperature.

2、本发明提供的用于燃料电池的冷却循环工艺中的所述第二循环回路还设有用于接收换热装置导出热量的第一储液箱。该冷却循环回路工艺可以将燃料电池内输出的热源中的热转换出去以达到再次利用的目的,能量转化效率高。2. The second circulation loop used in the fuel cell cooling circulation process provided by the present invention is further provided with a first liquid storage tank for receiving the heat exported by the heat exchange device. The cooling circulation loop process can convert the heat in the output heat source in the fuel cell to achieve the purpose of reuse, and the energy conversion efficiency is high.

3、本发明提供的用于燃料电池的冷却循环工艺中所述的第一循环回路设有热源液体净化处理装置可冷却处理燃料电池的热源液体出口温度T1低于M1时的冷却循环液,或是少量的冷却循环液,可实现燃料电池的快速启动,并且工作中,热源液体循环一段时间后会有杂质,所述热源液体冷却装置可净化杂质并冷却热源液体,当热源液体为水时这个装置即为去离子柱。3. The first circulation loop described in the cooling circulation process for fuel cells provided by the present invention is equipped with a heat source liquid purification treatment device to cool and treat the cooling circulation liquid when the heat source liquid outlet temperature T1 of the fuel cell is lower than M1, or It is a small amount of cooling circulating fluid, which can realize the rapid start-up of the fuel cell, and during operation, there will be impurities after the heat source liquid circulates for a period of time. The heat source liquid cooling device can purify impurities and cool the heat source liquid. When the heat source liquid is water, this The device is the deionization column.

4、本发明提供的用于燃料电池的冷却循环工艺中所述的第二循环回路可冷却处理燃料电池的热源液体出口温度T1高于M1而同时低于M2时的冷却循环液,或是大量的冷却循环液。将燃料电池产生的热进行利用。4. The second circulation loop described in the cooling circulation process for fuel cells provided by the present invention can cool and treat the cooling circulation liquid when the heat source liquid outlet temperature T1 of the fuel cell is higher than M1 and lower than M2 at the same time, or a large amount of cooling circulating fluid. The heat generated by the fuel cell is utilized.

5、本发明提供的用于燃料电池的冷却循环工艺中所述的换热装置为板式换热器,所述换热器内设有热源通道,所述热源通道的外围布置有冷却循环液通道,冷却循环液通过第一循环泵流入所述第二热冷却液箱。用于将热源通道内的热的液体降温并将热量带入第一储液箱。5. The heat exchange device described in the cooling circulation process for fuel cells provided by the present invention is a plate heat exchanger, and a heat source channel is arranged in the heat exchanger, and a cooling circulation liquid channel is arranged on the periphery of the heat source channel , the cooling circulating fluid flows into the second hot cooling fluid tank through the first circulating pump. It is used to cool down the hot liquid in the heat source channel and bring heat into the first liquid storage tank.

6、本发明提供的用于燃料电池的冷却循环工艺中所述的第二循环回路所设的散热装置与换热装置共同起作用,可冷却处理燃料电池的热源液体出口温度T1高于M2时的热源液体,或是大量的热源液体。能够保证燃料电池工作温度下热能的最大利用。6. The heat dissipation device and the heat exchange device set in the second circulation loop described in the cooling cycle process for fuel cells provided by the present invention work together to cool the fuel cell when the heat source liquid outlet temperature T1 is higher than M2 heat source liquid, or a large amount of heat source liquid. It can ensure the maximum utilization of heat energy at the working temperature of the fuel cell.

7、本发明提供的用于燃料电池的冷却循环工艺中所述的第二循环回路中所述换热装置与所述第二热冷却液箱之间设有第一循环泵,用于快速的冷却循环液泵入第一储液箱中。7. A first circulation pump is provided between the heat exchange device and the second heat coolant tank in the second circulation loop in the cooling circulation process for fuel cells provided by the present invention, for rapid The cooling circulating fluid is pumped into the first reservoir.

8、本发明提供的用于燃料电池的冷却循环工艺在所述温度传感器T1内设有温度检测装置和信号传输装置用于检测出口温度并传输给第二循环泵、节温器、换热器和散热器,从而实现对系统的冷却循环的控制。8. In the cooling circulation process for fuel cells provided by the present invention, a temperature detection device and a signal transmission device are provided in the temperature sensor T1 to detect the outlet temperature and transmit it to the second circulation pump, thermostat, and heat exchanger And the radiator, so as to realize the control of the cooling cycle of the system.

9、本发明提供的用于燃料电池的冷却循环工艺通过设置热源液体冷却装置在不影响温度控制的情况下提高热源液体的纯度,延长燃料电池寿命。9. The cooling circulation process for fuel cells provided by the present invention improves the purity of the heat source liquid without affecting the temperature control by setting the heat source liquid cooling device, and prolongs the life of the fuel cell.

10、本发明提供的冷却循环工艺可保证燃料电池的稳定运行基础上,使得燃料电池的寿命从5000h提高到10000h~20000h。10. The cooling circulation process provided by the present invention can ensure the stable operation of the fuel cell, so that the service life of the fuel cell can be increased from 5000h to 10000h-20000h.

附图说明Description of drawings

为了更清楚地说明本发明具体实施方式或现有技术中的技术方案,下面将对具体实施方式或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图是本发明的一些实施方式,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the specific implementation of the present invention or the technical solutions in the prior art, the following will briefly introduce the accompanying drawings that need to be used in the specific implementation or description of the prior art. Obviously, the accompanying drawings in the following description The drawings show some implementations of the present invention, and those skilled in the art can obtain other drawings based on these drawings without any creative work.

图1是本发明冷却循环回路系统图;Fig. 1 is the system diagram of the cooling cycle circuit of the present invention;

附图标记如下:The reference signs are as follows:

1-节温器,2-热源液体净化处理装置,3-换热器,4-第一储液箱,5-散热器,6-第一循环泵,7-第二储液箱,8-第二循环泵,9-燃料电池,10-第一温度传感器,11-第二温度传感器,12-第三温度传感器。1-thermostat, 2-heat source liquid purification treatment device, 3-heat exchanger, 4-first liquid storage tank, 5-radiator, 6-first circulation pump, 7-second liquid storage tank, 8- The second circulating pump, 9-fuel cell, 10-the first temperature sensor, 11-the second temperature sensor, 12-the third temperature sensor.

具体实施方式detailed description

下面结合附图对本发明进行说明。提供下述实施例是为了更好地进一步理解本发明,并不局限于所述最佳实施方式,不对本发明的内容和保护范围构成限制,任何人在本发明的启示下或是将本发明与其他现有技术的特征进行组合而得出的任何与本发明相同或相近似的产品,均落在本发明的保护范围之内。The present invention will be described below in conjunction with the accompanying drawings. The following examples are provided in order to further understand the present invention better, are not limited to the best implementation mode, and do not limit the content and protection scope of the present invention, anyone under the inspiration of the present invention or use the present invention Any product identical or similar to the present invention obtained by combining features of other prior art falls within the protection scope of the present invention.

实施例中未注明具体实验步骤或条件者,按照本领域内的文献所描述的常规实验步骤的操作或条件即可进行。所用试剂或仪器未注明生产厂商者,均为可以通过市购获得的常规试剂产品。If no specific experimental steps or conditions are indicated in the examples, it can be carried out according to the operation or conditions of the conventional experimental steps described in the literature in this field. The reagents or instruments used, whose manufacturers are not indicated, are all commercially available conventional reagent products.

说明:本发明中第一温度传感器显示的温度为T1,即燃料电池的热源液体出口温度,第二温度传感器显示的温度为T2,第三温度传感器显示的温度为T3。并设有两个温度阈值,分别为M1和M2,M1为燃料电池低温报警温度点;M2为燃料电池高温报警温度点。Explanation: In the present invention, the temperature displayed by the first temperature sensor is T1, that is, the outlet temperature of the heat source liquid of the fuel cell, the temperature displayed by the second temperature sensor is T2, and the temperature displayed by the third temperature sensor is T3. And there are two temperature thresholds, M1 and M2 respectively, M1 is the fuel cell low temperature alarm temperature point; M2 is the fuel cell high temperature alarm temperature point.

本发明提供的用于燃料电池的冷却循环回路在工作时,When the cooling circulation loop for the fuel cell provided by the present invention is in operation,

当T1<M1时,第二循环泵启动并以最低速度运行,第一循环泵不启动,循环的热源液体经节温器进入第一循环冷却回路,能够实现电池尽快升温,并且维持热源液体质量;When T1<M1, the second circulating pump starts and runs at the lowest speed, the first circulating pump does not start, and the circulating heat source liquid enters the first circulating cooling circuit through the thermostat, which can realize the battery heating up as soon as possible and maintain the quality of the heat source liquid ;

当M1<T1≤M2但时,热源液体通过第二循环回路,散热器不启动,只通过换热器进行换热,并根据燃料电池热源液体进口温度T3和换热循环第二储液箱内的热源液体温度T2对第二循环泵和第一循环泵进行调速,保证温度T3在燃料电池的允许范围内;When M1<T1≤M2, the heat source liquid passes through the second circulation loop, the radiator does not start, and only heat exchange is performed through the heat exchanger, and the second liquid storage tank is circulated according to the fuel cell heat source liquid inlet temperature T3 and heat exchange The temperature T2 of the heat source liquid adjusts the speed of the second circulation pump and the first circulation pump to ensure that the temperature T3 is within the allowable range of the fuel cell;

当T1>M2时,热源液体通过第二循环回路控制热源液体温度,在通过第二循环回路的换热器后,启动散热器,对循环的热源液体进一步强制散热,并根据燃料电池热源液体进口温度T3和换热循环第二储液箱内的热源液体温度对第二循环泵和第一循环泵进行调速,保证温度T3在燃料电池的允许范围内。When T1>M2, the heat source liquid passes through the second circulation loop to control the temperature of the heat source liquid, and after passing through the heat exchanger of the second circulation loop, the radiator is activated to further force the heat dissipation of the circulating heat source liquid, and according to the fuel cell heat source liquid inlet The temperature T3 and the temperature of the heat source liquid in the second liquid storage tank of the heat exchange cycle regulate the speed of the second circulation pump and the first circulation pump to ensure that the temperature T3 is within the allowable range of the fuel cell.

M1与M2的具体数值可以根据实际过程中燃料电池实际情况进行选择。The specific values of M1 and M2 can be selected according to the actual situation of the fuel cell in the actual process.

本发明中的燃料电池包括但不限于质子交换膜燃料电池、直接甲醇燃料电池、磷酸燃料电池、熔融碳酸盐燃料电池或高温固体氧化物燃料电池的一种或多种的组合。The fuel cell in the present invention includes but not limited to one or more combination of proton exchange membrane fuel cell, direct methanol fuel cell, phosphoric acid fuel cell, molten carbonate fuel cell or high temperature solid oxide fuel cell.

实施例1采用本发明冷却循环工艺的固定式质子交换膜燃料电池Example 1 The stationary proton exchange membrane fuel cell adopting the cooling circulation process of the present invention

该实施例使用一个10kW水冷质子交换膜燃料电池堆,单电池节数为120节。This embodiment uses a 10kW water-cooled proton exchange membrane fuel cell stack with 120 single cells.

该实施例中燃料电池低温报警温度点和燃料电池高温报警温度点分别为50℃和65℃。In this embodiment, the fuel cell low temperature alarm temperature point and the fuel cell high temperature alarm temperature point are 50° C. and 65° C. respectively.

首先,使用氮气对气体管道进行吹扫。然后为燃料电池两极分别供应氢气和空气,启动燃料电池及其辅机(包括循环泵)。接下来检测燃料电池的出水口温度T1、换热循环水温度T2和燃料电池进水口温度T3。当温度T1低于50℃时,启动第二循环泵,不启动第一循环泵和散热器的风扇。当温度T1高于50℃时且小于65℃时,启动第一循环泵,但不启动散热器,随着温度T1的逐渐升高,第一循环泵的速度也逐渐增加。当温度T1高于65℃时,启动第一循环泵并启动散热器,当温度T1低于61℃时,关闭散热器。First, the gas line is purged with nitrogen. Then supply hydrogen and air to the poles of the fuel cell respectively, and start the fuel cell and its auxiliary machines (including the circulation pump). Next, the temperature T1 of the water outlet of the fuel cell, the temperature T2 of the heat exchange circulating water, and the temperature T3 of the water inlet of the fuel cell are detected. When the temperature T1 is lower than 50° C., the second circulation pump is started, and the first circulation pump and the fan of the radiator are not started. When the temperature T1 is higher than 50° C. and lower than 65° C., the first circulation pump is started, but the radiator is not started. As the temperature T1 gradually increases, the speed of the first circulation pump gradually increases. When the temperature T1 is higher than 65°C, start the first circulation pump and start the radiator, and when the temperature T1 is lower than 61°C, turn off the radiator.

实施例2采用本发明冷却循环工艺的直接甲醇燃料电池Example 2 Direct Methanol Fuel Cell Using the Cooling Circulation Process of the Present Invention

该实施例使用一个5kW水冷直接甲醇燃料电池堆,单电池节数为60节。This embodiment uses a 5kW water-cooled direct methanol fuel cell stack with 60 single cells.

首先,使用氮气对气体管道进行吹扫。然后为燃料电池两极分别供应甲醇和空气,启动燃料电池及其辅机(包括循环泵)。接下来检测燃料电池的出水口温度T1、换热循环水温度T2和燃料电池进水口温度T3。当温度T1低于120℃时,启动第二循环泵和离子柱,不启动第一循环泵和散热器的风扇。当温度T1高于120℃时且小于135℃时,启动第一循环泵,但不启动散热器,随着温度T1的逐渐升高,第一循环泵的速度也逐渐增加。当温度T1高于135℃时,启动第一循环泵并启动散热器,当温度T1低于130℃时,关闭散热器。First, the gas line is purged with nitrogen. Then supply methanol and air to the two poles of the fuel cell, and start the fuel cell and its auxiliary machines (including the circulation pump). Next, the temperature T1 of the water outlet of the fuel cell, the temperature T2 of the heat exchange circulating water, and the temperature T3 of the water inlet of the fuel cell are detected. When the temperature T1 is lower than 120° C., the second circulation pump and the ion column are started, and the first circulation pump and the fan of the radiator are not started. When the temperature T1 is higher than 120° C. and lower than 135° C., the first circulation pump is activated, but the radiator is not activated. As the temperature T1 gradually increases, the speed of the first circulation pump gradually increases. When the temperature T1 is higher than 135°C, start the first circulation pump and start the radiator, and when the temperature T1 is lower than 130°C, turn off the radiator.

实施例3采用本发明冷却循环工艺的的高温固体氧化物燃料电池Example 3 High temperature solid oxide fuel cell using the cooling cycle process of the present invention

该实施例使用一个30kW高温固体氧化物燃料电池堆,单电池节数为350节。This embodiment uses a 30kW high temperature solid oxide fuel cell stack with 350 single cells.

首先,使用氮气对气体管道进行吹扫。然后为燃料电池两极分别供应氢气和空气,启动燃料电池及其辅机(包括循环泵)。接下来检测燃料电池的出水口温度T1、换热循环水温度T2和燃料电池进水口温度T3。当温度T1低于800℃时,启动第二循环泵,不启动第一循环泵和散热器的风扇。当温度T1高于800℃时且小于830℃时,启动第一循环泵,但不启动散热器,随着温度T1的逐渐升高,第一循环泵的速度也逐渐增加。当温度T1高于830℃时,启动第一循环泵并启动散热器,当温度T1低于820℃时,关闭散热器。First, the gas line is purged with nitrogen. Then supply hydrogen and air to the poles of the fuel cell respectively, and start the fuel cell and its auxiliary machines (including the circulation pump). Next, the temperature T1 of the water outlet of the fuel cell, the temperature T2 of the heat exchange circulating water, and the temperature T3 of the water inlet of the fuel cell are detected. When the temperature T1 is lower than 800° C., the second circulation pump is started, and the first circulation pump and the fan of the radiator are not started. When the temperature T1 is higher than 800° C. and lower than 830° C., the first circulation pump is activated, but the radiator is not activated. As the temperature T1 gradually increases, the speed of the first circulation pump gradually increases. When the temperature T1 is higher than 830°C, start the first circulation pump and start the radiator, and when the temperature T1 is lower than 820°C, turn off the radiator.

测试例test case

实施例1-5的采用本发明冷却循环工艺的燃料电池的效果验证Verification of the effect of the fuel cell using the cooling cycle process of the present invention in Examples 1-5

对比例1为采用中国专利文献CN 101587962A公开的冷却系统的质子交换膜燃料电池;对比例2为现有技术普通的燃料电池Comparative example 1 is a proton exchange membrane fuel cell using the cooling system disclosed in Chinese patent document CN 101587962A; Comparative example 2 is a common fuel cell in the prior art

实施例Example 运行的稳定性Stability of operation 电池寿命Battery Life 能量转化率energy conversion rate 11 稳定Stablize 3000030000 85%85% 22 稳定Stablize 2000020000 80%80% 33 稳定Stablize 1500015000 98%98% 对比例1Comparative example 1 稳定Stablize 8000h8000h 60%60% 对比例2Comparative example 2 不稳定unstable 5000h5000h 45%45%

实施例4.用于燃料电池的冷却循环回路Example 4. Cooling circulation loop for fuel cells

本实施提供了一种用于燃料电池的冷却循环回路,如图1所示,本发明提供的用于燃料电池9的冷却循环回路,包括并联设置的第一循环回路和第二循环回路,所述第一循环回路上设置有热源液体冷却装置2;所述第二循环回路上设置有换热装置。该技术方案可以根据燃料电池内输出的热源液体的温度选择启动第一循环回路或第二循环回路,换热装置可以将燃料电池内输出的热源中的热转换出去以达到再次利用的目的,能量转化效率高。This implementation provides a cooling cycle for fuel cells. As shown in FIG. 1, the cooling cycle for fuel cells 9 provided by the present invention includes a first cycle and a second cycle arranged in parallel, so A heat source liquid cooling device 2 is arranged on the first circulation loop; a heat exchange device is arranged on the second circulation loop. This technical solution can select to start the first circulation loop or the second circulation loop according to the temperature of the heat source liquid output in the fuel cell, and the heat exchange device can convert the heat in the heat source output in the fuel cell to achieve the purpose of reuse, energy High conversion efficiency.

所述第二循环回路上还设置有散热装置。所述散热装置与换热装置共同起作用,可冷却处理燃料电池9的热源液体出口温度T1高于M2时的热源液体,或是大量的热源液体。A cooling device is also provided on the second circulation loop. The heat dissipation device and the heat exchange device work together to cool down the heat source liquid when the outlet temperature T1 of the heat source liquid of the fuel cell 9 is higher than M2 , or a large amount of heat source liquid.

所述热源液体冷却装置2可冷却处理燃料电池的热源液体出口温度T1低于M1时的冷却循环液,或是少量的冷却循环液,可实现燃料电池的快速启动;并且工作中,热源液体循环一段时间后会有杂质,所述热源液体冷却装置2又起到净化的作用,本发明中当热源液体为水时这个装置即为去离子柱。The heat source liquid cooling device 2 can cool the cooling circulating fluid when the heat source liquid outlet temperature T1 of the fuel cell is lower than M1, or a small amount of cooling circulating fluid, which can realize the rapid start of the fuel cell; and during operation, the heat source liquid circulates After a period of time, there will be impurities, and the heat source liquid cooling device 2 plays the role of purification again. In the present invention, when the heat source liquid is water, this device is a deionization column.

还包括回路选择装置,用于控制流出所述燃料电池的冷却液进入第一循环回路或第二循环回路,所述第一储液箱4用于接收换热装置导出热量,从而传导出去以备不时之需,所述的第二循环回路可冷却处理燃料电池9的热源液体出口温度T1高于M1而同时低于M2时的热源液体,或是大量的热源液体。It also includes a circuit selection device, which is used to control the coolant flowing out of the fuel cell to enter the first circulation loop or the second circulation loop, and the first liquid storage tank 4 is used to receive the heat derived from the heat exchange device, so as to conduct it out for preparation When necessary, the second circulation loop can cool the heat source liquid when the heat source liquid outlet temperature T1 of the fuel cell 9 is higher than M1 and lower than M2 at the same time, or a large amount of heat source liquid.

所述换热装置与所述第一储液箱之间设有第一循环泵6,用于快速的冷却循环液泵入第一储液箱4中。所述换热装置为板式换热器3,所述换热器3内设有热源液体通道,所述热源液体通道的外围布置有冷却循环液通道,以使冷却循环液通过第一循环泵6流入所述第一储液箱4。用于将热源液体通道内的热的液体降温并将热量带入第一储液箱4。A first circulating pump 6 is provided between the heat exchange device and the first liquid storage tank, and is used for pumping cooling circulating fluid into the first liquid storage tank 4 rapidly. The heat exchange device is a plate heat exchanger 3, the heat source liquid channel is arranged in the heat exchanger 3, and the cooling circulating liquid channel is arranged on the periphery of the heat source liquid channel, so that the cooling circulating liquid passes through the first circulating pump 6 into the first storage tank 4. It is used to cool down the hot liquid in the heat source liquid channel and bring heat into the first liquid storage tank 4 .

还包括与燃料电池相连的第二储液箱7;It also includes a second liquid storage tank 7 connected to the fuel cell;

所述第一循环回路和所述第二循环回路在第二储液箱7的入口处汇合;The first circulation loop and the second circulation loop merge at the inlet of the second liquid storage tank 7;

所述回路选择装置通过第二循环泵8与燃料电池9相连。The circuit selection device is connected to the fuel cell 9 through the second circulating pump 8 .

所述回路选择装置为节温器1,所述散热装置为散热器5。The circuit selection device is a thermostat 1 , and the heat dissipation device is a radiator 5 .

所述燃料电池9热源液体出口处,所述第一储液箱4内以及燃料电池热源液体入口处,分别对应设有第一温度传感器10,第二温度传感器11,第三温度传感器12,所述第一温度传感器10内设有温度检测装置和信号传输装置用于检测出口温度并传输给第二循环泵8、节温器1、换热器3和散热器5。The outlet of the heat source liquid of the fuel cell 9, the inside of the first liquid storage tank 4 and the inlet of the fuel cell heat source liquid are respectively provided with a first temperature sensor 10, a second temperature sensor 11, and a third temperature sensor 12. The first temperature sensor 10 is provided with a temperature detection device and a signal transmission device for detecting the outlet temperature and transmitting it to the second circulating pump 8 , the thermostat 1 , the heat exchanger 3 and the radiator 5 .

本发明燃料电池9的冷却循环回路通过增设热源液体冷却装置2在不影响温度控制的情况下提高热源液体的纯度,延长燃料电池寿命。The cooling circulation circuit of the fuel cell 9 of the present invention improves the purity of the heat source liquid without affecting the temperature control by adding the heat source liquid cooling device 2 and prolongs the service life of the fuel cell.

本实施例中的第二循环回路中,大部分的循环热源液体通过板式换热器3和鼓风散热器5降温后回到第二储液箱7,即大部分循环热源液体通过节点1~节点4~节点5~节点3到达第二储液箱7,启用散热器5;小部分循环热源液体通过节点1~节点4~节点5~节点3到达第二储液箱7,不启用散热器5;极小部分循环热源液体通过节点1~节点2~节点3到达第二储液箱7。In the second circulation loop in this embodiment, most of the circulating heat source liquid passes through the plate heat exchanger 3 and the blast radiator 5 and then returns to the second liquid storage tank 7, that is, most of the circulating heat source liquid passes through nodes 1- Node 4~Node 5~Node 3 reaches the second liquid storage tank 7, and the radiator 5 is activated; a small part of the circulating heat source liquid reaches the second liquid storage tank 7 through Node 1~Node 4~Node 5~Node 3, and the radiator is not activated 5. A very small part of the circulating heat source liquid reaches the second liquid storage tank 7 through nodes 1-node 2-node 3.

本发明的冷却循环回路在应用于燃料电池9可保证燃料电池9的稳定运行基础上,使得燃料电池9的寿命从5000h提高到10000h~30000h。The cooling circulation loop of the present invention can increase the service life of the fuel cell 9 from 5000h to 10000h-30000h on the basis of being applied to the fuel cell 9 to ensure the stable operation of the fuel cell 9 .

显然以上所述仅为本发明的较佳实施例而已,并不用于限制本发明,尽管参照前述实施例对本发明进行了详细的说明,对于本领域的技术人员来说,其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换。这里无需也无法对所有的实施方式予以穷举。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。Apparently the above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Although the present invention has been described in detail with reference to the foregoing embodiments, those skilled in the art can still understand the foregoing The technical solutions described in the embodiments are modified, or equivalent replacements are made to some of the technical features. It is not necessary and impossible to exhaustively list all the implementation manners here. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included within the protection scope of the present invention.

Claims (12)

1.一种用于燃料电池的冷却循环工艺,其特征在于,使用1. A cooling cycle process for fuel cells, characterized in that, using 包括并联设置的第一循环回路和第二循环回路,所述第一循环回路上设置有热源液体冷却装置;所述第二循环回路上设置有换热装置。It includes a first circulation loop and a second circulation loop arranged in parallel, a heat source liquid cooling device is arranged on the first circulation loop; a heat exchange device is arranged on the second circulation loop. 2.根据权利要求1所述的冷却循环工艺,其特征在于,按如下步骤进行:2. cooling circulation process according to claim 1, is characterized in that, carries out as follows: (1)使燃料电池出口的热源液体经第二循环泵通入所述冷却循环回路;(1) Make the heat source liquid at the outlet of the fuel cell pass into the cooling circulation loop through the second circulation pump; (2)使所述冷却循环回路输出的热源液体流经第二储液箱,并进一步的流入燃料电池。(2) Make the heat source liquid output by the cooling circulation loop flow through the second liquid storage tank, and further flow into the fuel cell. 3.根据权利要求2所述的冷却循环工艺,其特征在于,所述第二循环回路上还设置有散热装置。3. The cooling circulation process according to claim 2, characterized in that, a cooling device is further arranged on the second circulation loop. 4.根据权利要3所述的冷却循环工艺,其特征在于,还包括,4. cooling cycle process according to claim 3, is characterized in that, also comprises, (1)设置第一温度阈值M1,(1) Setting the first temperature threshold M1, (2)当流出燃料电池的冷却液温度小于M1时,所述冷却液经第一循环回路返回所述燃料电池;(2) When the temperature of the coolant flowing out of the fuel cell is lower than M1, the coolant returns to the fuel cell through the first circulation loop; (3)当流出燃料电池的冷却液温度大于M1时,所述冷却液经第二循环回路返回所述燃料电池。(3) When the temperature of the coolant flowing out of the fuel cell is greater than M1, the coolant returns to the fuel cell through the second circulation loop. 5.根据权利要求4所述的燃料电池进行对冷却的方法,其特征在于,还设置有第二温度阈值M2,其中M1小于M2;5. The method for cooling the fuel cell according to claim 4, characterized in that a second temperature threshold M2 is also set, wherein M1 is smaller than M2; 当流出燃料电池的冷却液温度在M1和M2之间时,所述冷却液经所述换热装置冷却处理后返回燃料电池;When the temperature of the coolant flowing out of the fuel cell is between M1 and M2, the coolant is cooled by the heat exchange device and then returned to the fuel cell; 当流出燃料电池的冷却液温度大于M2时,所述冷却液经所述换热装置和所述散热装置冷却处理后返回燃料电池。When the temperature of the cooling liquid flowing out of the fuel cell is greater than M2, the cooling liquid returns to the fuel cell after being cooled by the heat exchange device and the heat dissipation device. 6.根据权利要求5所述的冷却循环工艺,其特征在于,还包括回路选择装置,用于控制流出所述燃料电池的冷却液进入第一循环回路或第二循环回路。6. The cooling cycle process according to claim 5, further comprising a circuit selection device for controlling the cooling liquid flowing out of the fuel cell into the first circulation loop or the second circulation loop. 7.根据权利要求6所述的冷却循环工艺,其特征在于,所述第二循环回路上还设有用于接收所述换热装置热量的第一储液箱。7 . The cooling circulation process according to claim 6 , wherein a first liquid storage tank for receiving heat from the heat exchange device is further provided on the second circulation loop. 7 . 8.根据权利要求7所述的冷却循环工艺,其特征在于,所述换热装置与所述第一储液箱之间设有第一循环泵。8. The cooling circulation process according to claim 7, wherein a first circulation pump is provided between the heat exchange device and the first liquid storage tank. 9.根据权利要求8所述的冷却循环工艺,其特征在于,所述换热装置为板式换热器,所述换热器内设有热源液体通道,所述热源液体通道的外围布置有冷却循环液通道,以使冷却循环液通过第一循环泵流入所述第一热储液箱。9. The cooling cycle process according to claim 8, characterized in that, the heat exchange device is a plate heat exchanger, a heat source liquid passage is arranged in the heat exchanger, and a cooling device is arranged around the heat source liquid passage. A circulation fluid channel, so that the cooling circulation fluid flows into the first heat storage tank through the first circulation pump. 10.根据权利要求9所述的冷却循环工艺,其特征在于,10. cooling cycle process according to claim 9, is characterized in that, 还包括与燃料电池相连的第二储液箱;A second liquid storage tank connected to the fuel cell is also included; 所述第一循环回路和所述第二循环回路在所述第二储液箱的入口处汇合;the first circulation loop and the second circulation loop join at the inlet of the second liquid storage tank; 所述回路选择装置通过第二循环泵与燃料电池相连。The circuit selection device is connected with the fuel cell through the second circulation pump. 11.根据权利要求10所述的冷却循环工艺,其特征在于,所述回路选择装置为节温器,所述散热装置为散热器。11. The cooling cycle process according to claim 10, characterized in that, the circuit selection device is a thermostat, and the heat dissipation device is a radiator. 12.根据权利要11所述的冷却循环工艺,其特征在于,所述燃料电池热源液体出口处,所述第一储液箱内以及燃料电池热源液体入口处,分别对应设有第一温度传感器,第二温度传感器,第三温度传感器,所述第一温度传感器内设有温度检测装置和信号传输装置用于检测出口温度并传输给第二循环泵、节温器、换热器和散热器。12. The cooling cycle process according to claim 11, characterized in that, at the outlet of the fuel cell heat source liquid, in the first liquid storage tank and at the inlet of the fuel cell heat source liquid, first temperature sensors are correspondingly provided , the second temperature sensor, the third temperature sensor, the first temperature sensor is equipped with a temperature detection device and a signal transmission device for detecting the outlet temperature and transmitting it to the second circulation pump, thermostat, heat exchanger and radiator .
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