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CN114839106A - Method, system, vehicle and medium for measuring hydrogen concentration of fuel cell - Google Patents

Method, system, vehicle and medium for measuring hydrogen concentration of fuel cell Download PDF

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CN114839106A
CN114839106A CN202110143956.7A CN202110143956A CN114839106A CN 114839106 A CN114839106 A CN 114839106A CN 202110143956 A CN202110143956 A CN 202110143956A CN 114839106 A CN114839106 A CN 114839106A
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hydrogen
hydrogen concentration
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CN114839106B (en
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赵兴旺
张国强
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Beijing Sinohytec Co Ltd
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    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N7/00Analysing materials by measuring the pressure or volume of a gas or vapour
    • G01N7/14Analysing materials by measuring the pressure or volume of a gas or vapour by allowing the material to emit a gas or vapour, e.g. water vapour, and measuring a pressure or volume difference
    • G01N7/16Analysing materials by measuring the pressure or volume of a gas or vapour by allowing the material to emit a gas or vapour, e.g. water vapour, and measuring a pressure or volume difference by heating the material
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    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract

The invention relates to the technical field of fuel cells, in particular to a method, a system, a vehicle and a medium for measuring the hydrogen concentration of a fuel cell; the method comprises the steps of carrying out gas-liquid separation on gas at the outlet of the hydrogen circulating pump, and heating the separated gas until the relative humidity is less than 100%; acquiring the temperature of the gas before heating and the saturated pressure at the corresponding temperature, the temperature of the heated gas and the saturated pressure, humidity and volume of the heated hydrogen at the corresponding temperature, and calculating to obtain the volume fraction of the heated hydrogen and the humidity RH of the gas before heating 9 If RH 9 Is more than 100 percent; calculating to obtain the final volume fraction of the hydrogen; if the gas humidity RH 9 Less than or equal to 100%, the volume fraction of hydrogen after heating is equal to the final volume fraction of hydrogen; the invention can realize the hydrogen concentration test with low development cost, simple structure and high reliability; through heating the gas after separating, can prevent the condensation of saturated vapor, guarantee the accuracy of measurement.

Description

一种燃料电池氢浓度的测量方法、系统、车辆以及介质A fuel cell hydrogen concentration measurement method, system, vehicle and medium

技术领域technical field

本发明涉及燃料电池技术领域,具体涉及一种燃料电池氢浓度的测量方法、 系统、车辆以及介质。The present invention relates to the technical field of fuel cells, in particular to a method, system, vehicle and medium for measuring hydrogen concentration of fuel cells.

背景技术Background technique

质子交换膜燃料电池的工作原理是氢气和氧气发生电化学反应,生成水的 同时输出电能。由于燃料电池单体的电压通常小于1V,在实际应用时,需要将 上百片单体串联组成燃料电池电堆,并匹配相应的外围附件,构成燃料电池系 统。The working principle of proton exchange membrane fuel cell is that hydrogen and oxygen undergo electrochemical reaction to generate water and output electricity at the same time. Since the voltage of the fuel cell is usually less than 1V, in practical application, it is necessary to connect hundreds of cells in series to form a fuel cell stack, and match the corresponding peripheral accessories to form a fuel cell system.

氢气是燃料电池电化学反应的反应物之一,现有的燃料电池系统中,在阳 极侧通常借助氢气循环泵或者引射器进行氢气再循环,提高氢气的利用率,但 其浓度的大小严重影响电堆的输出性能和寿命,由于阳极侧通常携带有液态水, 现有的氢浓度传感器容易受到液态水影响导致功能失效,因此需要开发适当的 技术监测阳极侧的氢气浓度。Hydrogen is one of the reactants in the electrochemical reaction of fuel cells. In the existing fuel cell system, hydrogen is usually recycled on the anode side with the help of a hydrogen circulation pump or an ejector to improve the utilization rate of hydrogen, but its concentration is serious. It affects the output performance and life of the stack. Since the anode side usually carries liquid water, the existing hydrogen concentration sensor is easily affected by liquid water and leads to functional failure. Therefore, it is necessary to develop an appropriate technology to monitor the hydrogen concentration on the anode side.

发明内容SUMMARY OF THE INVENTION

本发明所要解决的技术问题是:提供一种结构简单,成本低廉的燃料电池 氢浓度的测量方法、系统、车辆以及介质。The technical problem to be solved by the present invention is to provide a fuel cell hydrogen concentration measurement method, system, vehicle and medium with simple structure and low cost.

为了解决上述技术问题,本发明采用的第一种技术方案为:In order to solve the above-mentioned technical problems, the first technical scheme adopted by the present invention is:

一种燃料电池氢浓度的测量方法,包括A method for measuring hydrogen concentration in a fuel cell, comprising:

对氢气循环泵出口的气体进行气液分离,并对分离后的气体进行加热,加 热后的气体的相对湿度小于100%;获取气体加热前的温度T7和对应温度下的饱 和气压psat(T7);Gas-liquid separation is performed on the gas at the outlet of the hydrogen circulation pump, and the separated gas is heated, and the relative humidity of the heated gas is less than 100%; the temperature T 7 before the gas heating and the saturated pressure p sat ( T7 );

获取加热后气体的温度T10、压力p10、湿度RH10、对应温度下的饱和气压 psat(T10)、加热后氢气体积xH2,11和加热后氢气体积分数xw,11,所述加热后氢气 体积分数xw,11计算方式为:Obtain the temperature T 10 , the pressure p 10 , the humidity RH 10 , the saturation pressure p sat (T 10 ) at the corresponding temperature, the hydrogen volume x H2,11 after heating, and the hydrogen volume fraction x w,11 after heating, so The calculation method of the hydrogen volume fraction x w, 11 after the heating is:

Figure BDA0002930252380000021
Figure BDA0002930252380000021

根据加热后的气体温度T10和湿度RH10获取加热前的气体湿度RH9,所述气 体湿度RH9计算方式为:The gas humidity RH 9 before heating is obtained according to the heated gas temperature T 10 and the humidity RH 10 , and the calculation method of the gas humidity RH 9 is:

Figure BDA0002930252380000022
Figure BDA0002930252380000022

若RH9>100%;则最终氢气体积分数xH2,final的计算方式为:If RH 9 >100%; then the final hydrogen volume fraction x H2, the final calculation method is:

Figure BDA0002930252380000023
Figure BDA0002930252380000023

若气体湿度RH9≤100%,则加热后氢气体积分数xw,11等于最终氢气体积分数xH2,finalIf the gas humidity RH 9 ≤ 100%, the hydrogen volume fraction x w,11 after heating is equal to the final hydrogen volume fraction x H2,final .

为了解决上述技术问题,本发明采用的第二种技术方案为:In order to solve the above-mentioned technical problems, the second technical scheme adopted by the present invention is:

一种电池氢浓度测量系统,包括测量回路和依次设置在测量回路上的气液 分离组件、加热件、温压湿传感器以及氢气浓度传感器;A battery hydrogen concentration measurement system, comprising a measurement loop and a gas-liquid separation component, a heating element, a temperature, pressure and humidity sensor and a hydrogen concentration sensor arranged in sequence on the measurement loop;

所述加热件之前的测量回路上设置有温压传感器。A temperature and pressure sensor is arranged on the measurement loop before the heating element.

为了解决上述技术问题,本发明采用的第三种技术方案为:In order to solve the above-mentioned technical problems, the third technical scheme adopted by the present invention is:

一种车辆,包括燃料电池,所述燃料电池包括氢气循环泵,所述氢气循环 泵包括进口和出口,还包括权利上述的电池氢浓度测量系统;A vehicle, comprising a fuel cell, the fuel cell comprising a hydrogen circulation pump, the hydrogen circulation pump comprising an inlet and an outlet, and the battery hydrogen concentration measurement system described above;

所述电池氢浓度测量系统的测量回路并联在氢气循环泵包括进口和出口上;The measurement loop of the battery hydrogen concentration measurement system is connected in parallel with the hydrogen circulation pump including the inlet and the outlet;

具有所述气液分离组件的测量回路的一端连接上进口上。One end of the measurement loop with the gas-liquid separation assembly is connected to the inlet.

为了解决上述技术问题,本发明采用的第四种技术方案为:In order to solve the above-mentioned technical problems, the fourth technical scheme adopted by the present invention is:

一种介质,其上存储有计算机程序,该计算机程序被处理器执行时实现如 上述的燃料电池氢浓度的测量方法。A medium having stored thereon a computer program that, when executed by a processor, implements the method for measuring the hydrogen concentration of a fuel cell as described above.

本发明的有益效果在于:通过本发明的电池氢浓度测量系统以及方法,能 够实现开发成本低、结构简单、可靠性高的氢浓度测试;克服现有技术中为了 实现测量导致系统复杂,成本高的问题;通过对分离后的气体进行加热,加热 后的气体的相对湿度小于100%提高饱和蒸气压,防止饱和水蒸气的冷凝,保证 测量的准确性。The beneficial effects of the present invention are as follows: through the battery hydrogen concentration measurement system and method of the present invention, a hydrogen concentration test with low development cost, simple structure and high reliability can be realized; and the system is complicated and the cost is high in order to achieve measurement in the prior art. By heating the separated gas, the relative humidity of the heated gas is less than 100%, increasing the saturated vapor pressure, preventing the condensation of saturated water vapor, and ensuring the accuracy of the measurement.

附图说明Description of drawings

图1为本发明具体实施方式的一种燃料电池氢浓度的测量系统的结构示意 图;1 is a schematic structural diagram of a fuel cell hydrogen concentration measurement system according to a specific embodiment of the present invention;

标号说明:1、控制阀;2、氢气循环泵;3、电磁吹扫阀;4、电堆;5、调 压阀;6、空压机;7、温压传感器;8、分水件;9、防水透气件;10、温压湿 传感器;11、氢气浓度传感器;12、加热件;13、测量回路。Label description: 1. Control valve; 2. Hydrogen circulation pump; 3. Electromagnetic purge valve; 4. Electric stack; 5. Pressure regulating valve; 6. Air compressor; 7. Temperature and pressure sensor; 8. Water separation piece; 9. Waterproof and breathable parts; 10. Temperature, pressure and humidity sensor; 11. Hydrogen concentration sensor; 12. Heating element; 13. Measuring circuit.

具体实施方式Detailed ways

为详细说明本发明的技术内容、所实现目的及效果,以下结合实施方式并 配合附图予以说明。In order to describe in detail the technical content, achieved objects and effects of the present invention, the following descriptions are given with reference to the embodiments and the accompanying drawings.

请参照图1,一种燃料电池氢浓度的测量方法,包括Please refer to FIG. 1, a method for measuring the hydrogen concentration of a fuel cell, comprising:

对氢气循环泵出口的气体进行气液分离,并对分离后的气体进行加热,加 热后的气体的相对湿度小于100%;获取气体加热前的温度T7和对应温度下的饱 和气压psat(T7);Gas-liquid separation is performed on the gas at the outlet of the hydrogen circulation pump, and the separated gas is heated, and the relative humidity of the heated gas is less than 100%; the temperature T 7 before the gas heating and the saturated pressure p sat ( T7 );

获取加热后气体的温度T10、压力p10、湿度RH10、对应温度下的饱和气压 psat(T10)、加热后氢气体积xH2,11和加热后氢气体积分数xw,11,所述加热后氢气 体积分数xw,11计算方式为:Obtain the temperature T 10 , the pressure p 10 , the humidity RH 10 , the saturation pressure p sat (T 10 ) at the corresponding temperature, the hydrogen volume x H2,11 after heating, and the hydrogen volume fraction x w,11 after heating, so The calculation method of the hydrogen volume fraction x w, 11 after the heating is:

Figure BDA0002930252380000031
Figure BDA0002930252380000031

根据加热后的气体温度T10和湿度RH10获取加热前的气体湿度RH9,所述气 体湿度RH9计算方式为:The gas humidity RH 9 before heating is obtained according to the heated gas temperature T 10 and the humidity RH 10 , and the calculation method of the gas humidity RH 9 is:

Figure BDA0002930252380000032
Figure BDA0002930252380000032

若RH9>100%;则最终氢气体积分数xH2,final的计算方式为:If RH 9 >100%; then the final hydrogen volume fraction x H2, the final calculation method is:

Figure BDA0002930252380000043
Figure BDA0002930252380000043

若气体湿度RH9≤100%,则加热后氢气体积分数xw,11等于最终氢气体积分数xH2,finalIf the gas humidity RH 9 ≤ 100%, the hydrogen volume fraction x w,11 after heating is equal to the final hydrogen volume fraction x H2,final .

进一步的,所述气液分离前和气液分离后的流量比小于5%。Further, the flow ratio before the gas-liquid separation and after the gas-liquid separation is less than 5%.

从上述描述可知,通过气液分离前和气液分离后的流量比小于5%,避免测 量过程对系统正常运行的影响;可选的,如果流量比小于5%,则测量回路中的 流量可以在保证安全的情况下排放到大气中。It can be seen from the above description that the flow ratio before gas-liquid separation and after gas-liquid separation is less than 5% to avoid the influence of the measurement process on the normal operation of the system; optionally, if the flow ratio is less than 5%, the flow in the measurement loop can be Released to the atmosphere in a safe manner.

进一步的,所述气液分离前和气液分离后的流量比为1%。Further, the flow ratio before the gas-liquid separation and after the gas-liquid separation is 1%.

进一步的,还包括最终氮气体积分数xN2;若RH9>100%;则最终氮气体积 分数xN2计算方式为:Further, it also includes the final nitrogen volume fraction x N2 ; if RH 9 >100%; the calculation method of the final nitrogen volume fraction x N2 is:

Figure BDA0002930252380000041
Figure BDA0002930252380000041

若气体湿度RH9≤100%,则最终氮气体积分数xN2计算方式为:If the gas humidity RH 9 ≤ 100%, the final nitrogen volume fraction x N2 is calculated as:

xN2=1-xH2,final-xw,11x N2 = 1-x H2, final -x w, 11 .

一种电池氢浓度测量系统,包括测量回路和依次设置在测量回路上的气液 分离组件、加热件、温压湿传感器以及氢气浓度传感器;A battery hydrogen concentration measurement system, comprising a measurement loop and a gas-liquid separation component, a heating element, a temperature, pressure and humidity sensor and a hydrogen concentration sensor arranged in sequence on the measurement loop;

所述加热件之前的测量回路上设置有温压传感器。A temperature and pressure sensor is arranged on the measurement loop before the heating element.

进一步的,所述气液分离组件包括沿测量回路依次设置的分水件和防水透 气伴。Further, the gas-liquid separation assembly includes a water dividing member and a waterproof and air-permeable partner arranged in sequence along the measurement circuit.

进一步的,所述氢气浓度传感器之后的测量回路上还设置有流量传感器。Further, a flow sensor is also provided on the measurement loop after the hydrogen concentration sensor.

从上述描述可知,通过流量传感器的设置,能够精确的计算气体组分。It can be seen from the above description that the gas composition can be accurately calculated by setting the flow sensor.

进一步的,所述氢气浓度传感器之后的测量回路上还设置有调压件。Further, a pressure regulating member is also provided on the measurement loop after the hydrogen concentration sensor.

从上述描述可知,通过调压件的设置,能够对测量回路中流量的精确控制, 满足回路中的流量与循环回路中的流量比小于5%。It can be seen from the above description that, through the arrangement of the pressure regulating element, the flow rate in the measurement loop can be precisely controlled, so that the ratio of the flow rate in the loop to the flow rate in the circulation loop is less than 5%.

一种车辆,包括燃料电池,所述燃料电池包括氢气循环泵,所述氢气循环 泵包括进口和出口,还包括上述的电池氢浓度测量系统;A vehicle, comprising a fuel cell, the fuel cell comprising a hydrogen circulation pump, the hydrogen circulation pump comprising an inlet and an outlet, and the above-mentioned battery hydrogen concentration measurement system;

所述电池氢浓度测量系统的测量回路并联在氢气循环泵包括进口和出口上;The measurement loop of the battery hydrogen concentration measurement system is connected in parallel with the hydrogen circulation pump including the inlet and the outlet;

具有所述气液分离组件的测量回路的一端连接上进口上。One end of the measurement loop with the gas-liquid separation assembly is connected to the inlet.

一种介质,其上存储有计算机程序,该计算机程序被处理器执行时实现上 述的燃料电池氢浓度的测量方法。A medium having stored thereon a computer program that, when executed by a processor, implements the above-described method for measuring hydrogen concentration in a fuel cell.

从上述描述可知,通过本发明的电池氢浓度测量系统以及方法,能够实现 开发成本低、结构简单、可靠性高的氢浓度测试;克服现有技术中为了实现测 量导致系统复杂,成本高的问题。As can be seen from the above description, the battery hydrogen concentration measurement system and method of the present invention can realize the hydrogen concentration measurement with low development cost, simple structure and high reliability; and overcome the problems of complicated system and high cost in the prior art in order to realize the measurement. .

实施例一Example 1

一种燃料电池氢浓度的测量方法,包括A method for measuring hydrogen concentration in a fuel cell, comprising:

对氢气循环泵出口的气体进行气液分离,并对分离后的气体进行加热,加 热后的气体的相对湿度小于100%或小于80%;获取气体加热前的温度T7和 对应温度下的饱和气压psat(T7);Gas-liquid separation is performed on the gas at the outlet of the hydrogen circulating pump, and the separated gas is heated. The relative humidity of the heated gas is less than 100% or less than 80%; the temperature T7 before gas heating and the saturation at the corresponding temperature are obtained. air pressure p sat (T 7 );

获取加热后气体的温度T10、压力p10、湿度RH10、对应温度下的饱和气压 psat(T10)、加热后氢气体积xH2,11和加热后氢气体积分数xw,11,所述加热后氢气 体积分数xw,11计算方式为:Obtain the temperature T 10 , the pressure p 10 , the humidity RH 10 , the saturation pressure p sat (T 10 ) at the corresponding temperature, the hydrogen volume x H2,11 after heating, and the hydrogen volume fraction x w,11 after heating, so The calculation method of the hydrogen volume fraction x w, 11 after the heating is:

Figure BDA0002930252380000051
Figure BDA0002930252380000051

根据加热后的气体温度T10和湿度RH10获取加热前的气体湿度RH9(公式中 采用T7是因为经过气液分离前后,测量回路内的温度变化极小,可以忽略不计, 视作等同,因此直接采用作为气液分离后的温度使用),所述气体湿度RH9计算 方式为:Obtain the gas humidity RH 9 before heating according to the gas temperature T 10 after heating and humidity RH 10 (T 7 is used in the formula because the temperature change in the measurement loop is very small before and after gas-liquid separation, which can be ignored and regarded as equivalent , so it is directly used as the temperature after gas-liquid separation), and the calculation method of the gas humidity RH 9 is:

Figure BDA0002930252380000052
Figure BDA0002930252380000052

若RH9>100%;则最终氢气体积分数xH2,final的计算方式为:If RH 9 >100%; then the final hydrogen volume fraction x H2, the final calculation method is:

Figure BDA0002930252380000061
Figure BDA0002930252380000061

若气体湿度RH9≤100%,则加热后氢气体积分数xw,11等于最终氢气体积分数xH2,finalIf the gas humidity RH 9 ≤ 100%, the hydrogen volume fraction x w,11 after heating is equal to the final hydrogen volume fraction x H2,final .

所述气液分离前和气液分离后的流量比为1%。The flow ratio before the gas-liquid separation and after the gas-liquid separation is 1%.

还包括最终氮气体积分数xN2;若RH9>100%;则最终氮气体积分数xN2计算方式为:It also includes the final nitrogen volume fraction x N2 ; if RH 9 >100%; then the final nitrogen volume fraction x N2 is calculated as:

Figure BDA0002930252380000062
Figure BDA0002930252380000062

若气体湿度RH9≤100%,则最终氮气体积分数xN2计算方式为:If the gas humidity RH 9 ≤ 100%, the final nitrogen volume fraction x N2 is calculated as:

xN2=1-xH2,final-xw,11x N2 = 1-x H2, final -x w, 11 .

其中in

参照图1,T7为温压传感器7处的温度,psat(T7)为温压传感器7对应温度下 的饱和气压;Referring to FIG. 1 , T 7 is the temperature at the temperature and pressure sensor 7 , and p sat (T 7 ) is the saturated air pressure at the corresponding temperature of the temperature and pressure sensor 7 ;

T10、p10、RH10为温压湿传感器10处的温度、压力和湿度,psat(T10) 为温压湿传感器10对应温度下的饱和气压;T 10 , p 10 , and RH 10 are the temperature, pressure, and humidity at the temperature, pressure, and humidity sensor 10 , and p sat (T 10 ) is the saturated air pressure at the corresponding temperature of the temperature, pressure, and humidity sensor 10 ;

xH2,11为氢气浓度传感器处获得加热后氢气体积;x H2 , 11 is the hydrogen volume after heating obtained at the hydrogen concentration sensor;

RH9为防水透气件9处的气体湿度。RH 9 is the gas humidity at the waterproof vent 9 .

实施例二Embodiment 2

参照图1,一种电池氢浓度测量系统,包括测量回路13和依次设置在测量 回路13上的气液分离组件、加热件12、温压湿传感器10以及氢气浓度传感器 11;Referring to Fig. 1, a battery hydrogen concentration measurement system includes a measurement loop 13 and a gas-liquid separation assembly, a heating element 12, a temperature, pressure and humidity sensor 10 and a hydrogen concentration sensor 11 arranged in sequence on the measurement loop 13;

所述加热件之前的测量回路13上设置有温压传感器7。A temperature and pressure sensor 7 is arranged on the measurement loop 13 before the heating element.

所述气液分离组件包括沿测量回路13依次设置的分水件8和防水透气件9。The gas-liquid separation assembly includes a water dividing member 8 and a waterproof ventilation member 9 arranged in sequence along the measuring circuit 13 .

所述氢气浓度传感器11之后的测量回路13上还设置有流量传感器。A flow sensor is also provided on the measurement loop 13 after the hydrogen concentration sensor 11 .

所述氢气浓度传感器11之后的测量回路13上还设置有调压件。A pressure regulating member is also provided on the measurement circuit 13 after the hydrogen concentration sensor 11 .

其中in

所述分水件8为SMC型号的分水装置,可以选择将气体中液态水颗粒直径 大于50um的去除;所述防水透气件9为防水透气阀,理论上,可以只允许氢气、 氮气、水蒸气等气体通过,不允许液态水颗粒通过,其采用的e-PTFE薄膜材料 孔径在0.1-10um之间,液态水颗粒一般大于这个范围,而气体分子的直径在 0.4nm,且由于薄膜材料的高接触角等特性,可以有效实现气水分离。Described water divider 8 is the water divider of SMC model, can choose to remove the liquid water particle diameter greater than 50um in gas; Described waterproof breathable member 9 is waterproof breathable valve, in theory, can only allow hydrogen, nitrogen, water Gases such as steam pass through, and liquid water particles are not allowed to pass through. The e-PTFE film material used has a pore size between 0.1-10um. The liquid water particles are generally larger than this range, and the diameter of the gas molecules is 0.4nm. High contact angle and other characteristics can effectively achieve gas-water separation.

实施例三Embodiment 3

参照图1,一种车辆,包括燃料电池,所述燃料电池包括控制阀1、氢气循 环泵2、电磁吹扫阀3、电堆4、调压阀5、空压机6,所述氢气通过控制阀1进 入到电堆4内,所述空气通过空压机6进入到电堆4内,所述电磁吹扫阀3控 制反应生成物的排出,所述调压阀5控制电堆4的压力;所述氢气循环泵2包 括进口和出口,1, a vehicle includes a fuel cell, the fuel cell includes a control valve 1, a hydrogen circulation pump 2, an electromagnetic purge valve 3, an electric stack 4, a pressure regulating valve 5, and an air compressor 6, the hydrogen gas passes through The control valve 1 enters into the stack 4, the air enters into the stack 4 through the air compressor 6, the electromagnetic purge valve 3 controls the discharge of reaction products, and the pressure regulating valve 5 controls the discharge of the stack 4. pressure; the hydrogen circulation pump 2 includes an inlet and an outlet,

还包括实施例一所述的电池氢浓度测量系统;Also includes the battery hydrogen concentration measurement system described in Embodiment 1;

所述电池氢浓度测量系统的测量回路13并联在氢气循环泵2包括进口和出 口上;The measurement loop 13 of the battery hydrogen concentration measurement system is connected in parallel with the hydrogen circulation pump 2 including the inlet and the outlet;

具有所述气液分离组件的测量回路13的一端连接上进口上。One end of the measuring circuit 13 with the gas-liquid separation assembly is connected to the inlet.

所述测量回路13以靠近氢气循环泵2的出口为起始端,靠近氢气循环泵2 的进口为末尾端,所述测量回路13从起始端到末尾端依次设置有温压传感器7、 分水件8、防水透气件9、加热件12、温压湿传感器10以及氢气浓度传感器11。The measuring loop 13 is set close to the outlet of the hydrogen circulation pump 2 as the starting end, and the inlet close to the hydrogen circulating pump 2 is the ending end. 8. The waterproof ventilation member 9 , the heating member 12 , the temperature, pressure and humidity sensor 10 and the hydrogen concentration sensor 11 .

实施例四Embodiment 4

一种介质,其上存储有计算机程序,该计算机程序被处理器执行时实现如 实施例一所述的燃料电池氢浓度的测量方法。A medium on which a computer program is stored, and when the computer program is executed by a processor, implements the method for measuring the hydrogen concentration of a fuel cell as described in the first embodiment.

以上所述仅为本发明的实施例,并非因此限制本发明的专利范围,凡是利 用本发明说明书及附图内容所作的等同变换,或直接或间接运用在相关的技术 领域,均同理包括在本发明的专利保护范围内。The above descriptions are only examples of the present invention, and are not intended to limit the scope of the patent of the present invention. Any equivalent transformations made by using the contents of the description and drawings of the present invention, or directly or indirectly applied in related technical fields, are similarly included in the within the scope of patent protection of the present invention.

Claims (10)

1.一种燃料电池氢浓度的测量方法,其特征在于,包括1. a measuring method of hydrogen concentration of fuel cell, is characterized in that, comprises 对氢气循环泵出口的气体进行气液分离,并对分离后的气体进行加热,加热后的气体的相对湿度小于100%;获取气体加热前的温度T7和对应温度下的饱和气压psat(T7);Gas-liquid separation is performed on the gas at the outlet of the hydrogen circulation pump, and the separated gas is heated, and the relative humidity of the heated gas is less than 100%; the temperature T 7 before the gas heating and the saturated pressure p sat ( T7 ); 获取加热后气体的温度T10、压力p10、湿度RH10、对应温度下的饱和气压psat(T10)、加热后氢气体积xH2,11和加热后氢气体积分数xw,11,所述加热后氢气体积分数xw,11计算方式为:Obtain the temperature T 10 , the pressure p 10 , the humidity RH 10 , the saturation pressure p sat (T 10 ) at the corresponding temperature, the hydrogen volume x H2,11 after heating, and the hydrogen volume fraction x w,11 after heating, so The calculation method of the hydrogen volume fraction x w, 11 after the heating is:
Figure FDA0002930252370000011
Figure FDA0002930252370000011
根据加热后的气体温度T10和湿度RH10获取加热前的气体湿度RH9,所述气体湿度RH9计算方式为:The gas humidity RH 9 before heating is obtained according to the heated gas temperature T 10 and the humidity RH 10 , and the calculation method of the gas humidity RH 9 is:
Figure FDA0002930252370000012
Figure FDA0002930252370000012
若RH9>100%;则最终氢气体积分数xH2,final的计算方式为:If RH 9 >100%; then the final hydrogen volume fraction x H2, the final calculation method is:
Figure FDA0002930252370000013
Figure FDA0002930252370000013
若气体湿度RH9≤100%,则加热后氢气体积分数xw,11等于最终氢气体积分数xH2,finalIf the gas humidity RH 9 ≤ 100%, the hydrogen volume fraction x w,11 after heating is equal to the final hydrogen volume fraction x H2,final .
2.根据权利要求1所述的燃料电池氢浓度的测量方法,其特征在于,所述气液分离前和气液分离后的流量比小于5%。2 . The method for measuring hydrogen concentration of a fuel cell according to claim 1 , wherein the flow ratio before the gas-liquid separation and after the gas-liquid separation is less than 5%. 3 . 3.根据权利要求2所述的燃料电池氢浓度的测量方法,其特征在于,所述气液分离前和气液分离后的流量比为1%。3 . The method for measuring hydrogen concentration of a fuel cell according to claim 2 , wherein the flow ratio before the gas-liquid separation and after the gas-liquid separation is 1%. 4 . 4.根据权利要求1所述的燃料电池氢浓度的测量方法,其特征在于,还包括最终氮气体积分数xN2;若RH9>100%;则最终氮气体积分数xN2计算方式为:4. The method for measuring the hydrogen concentration of a fuel cell according to claim 1, further comprising: the final nitrogen volume fraction x N2 ; if RH 9 >100%; the calculation method of the final nitrogen volume fraction x N2 is:
Figure FDA0002930252370000014
Figure FDA0002930252370000014
若气体湿度RH9≤100%,则最终氮气体积分数xN2计算方式为:If the gas humidity RH 9 ≤ 100%, the final nitrogen volume fraction x N2 is calculated as: xN2=1-xH2,final-xw,11x N2 = 1-x H2, final -x w, 11 .
5.一种电池氢浓度测量系统,其特征在于,包括测量回路和依次设置在测量回路上的气液分离组件、加热件、温压湿传感器以及氢气浓度传感器;5. A battery hydrogen concentration measurement system, characterized in that it comprises a measurement loop and a gas-liquid separation assembly, a heating element, a temperature, pressure and humidity sensor and a hydrogen concentration sensor sequentially arranged on the measurement loop; 所述加热件之前的测量回路上设置有温压传感器。A temperature and pressure sensor is arranged on the measurement loop before the heating element. 6.根据权利要求5所述的电池氢浓度测量系统,其特征在于,所述气液分离组件包括沿测量回路依次设置的分水件和防水透气件。6 . The battery hydrogen concentration measurement system according to claim 5 , wherein the gas-liquid separation component comprises a water separation member and a waterproof ventilation member arranged in sequence along the measurement loop. 7 . 7.根据权利要求5所述的电池氢浓度测量系统,其特征在于,所述氢气浓度传感器之后的测量回路上还设置有流量传感器。7 . The battery hydrogen concentration measurement system according to claim 5 , wherein a flow sensor is further provided on the measurement loop after the hydrogen concentration sensor. 8 . 8.根据权利要求5所述的电池氢浓度测量系统,其特征在于,所述氢气浓度传感器之后的测量回路上还设置有调压件。8 . The battery hydrogen concentration measurement system according to claim 5 , wherein a pressure regulating member is further provided on the measurement loop after the hydrogen concentration sensor. 9 . 9.一种车辆,包括燃料电池,所述燃料电池包括氢气循环泵,所述氢气循环泵包括进口和出口,其特征在于,还包括权利要求5-8任意一项所述的电池氢浓度测量系统;9. A vehicle, comprising a fuel cell, the fuel cell comprising a hydrogen circulation pump, the hydrogen circulation pump comprising an inlet and an outlet, characterized in that, further comprising the battery hydrogen concentration measurement according to any one of claims 5-8 system; 所述电池氢浓度测量系统的测量回路并联在氢气循环泵包括进口和出口上;The measurement loop of the battery hydrogen concentration measurement system is connected in parallel with the hydrogen circulation pump including the inlet and the outlet; 具有所述气液分离组件的测量回路的一端连接上进口上。One end of the measurement loop with the gas-liquid separation assembly is connected to the inlet. 10.一种介质,其上存储有计算机程序,其特征在于,该计算机程序被处理器执行时实现如权利要求1-4任意一项所述的燃料电池氢浓度的测量方法。10. A medium on which a computer program is stored, characterized in that, when the computer program is executed by a processor, the method for measuring hydrogen concentration of a fuel cell according to any one of claims 1-4 is implemented.
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