CN115441017A - Water-cooled fuel cell stack low-temperature starting method based on optimal energy efficiency - Google Patents
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Abstract
本发明提供一种基于能效最优的水冷型燃料电池电堆低温启动方法,属于新能源发电技术领域,设置电堆自热启动所需最低温度、最大时间限度和电堆低温启动成功时的电子负载电流密度,开启电加热丝电源调至功率最大;确定外辅多约束预测控制器的被控变量、控制变量和约束条件,实时调整电加热丝功率,直至电堆温度达到自热启动所需最低温度,关闭电源;确定自热多约束预测控制器的被控变量、控制变量和约束条件,实时调整电子负载电流密度,直至达到电堆低温启动成功时的电子负载电流密度,低温启动成功。本发明将电堆低温启动时间控制在安全范围内,安全可靠,同时能量利用最大化,降低成本,实现快速稳定、能效最优的水冷型燃料电池低温启动控制。
The invention provides a water-cooled fuel cell stack low-temperature start-up method based on optimal energy efficiency, which belongs to the technical field of new energy power generation. Load current density, turn on the power supply of the electric heating wire and adjust to the maximum power; determine the controlled variable, control variable and constraint conditions of the external auxiliary multi-constraint predictive controller, and adjust the power of the electric heating wire in real time until the stack temperature reaches the requirement for self-heating start Turn off the power at the lowest temperature; determine the controlled variables, control variables and constraints of the self-heating multi-constraint predictive controller, and adjust the electronic load current density in real time until it reaches the electronic load current density when the stack starts successfully at low temperature, and the low temperature start is successful. The invention controls the low-temperature start-up time of the electric stack within a safe range, is safe and reliable, maximizes energy utilization, reduces costs, and realizes fast, stable, and energy-efficient low-temperature start-up control of the water-cooled fuel cell.
Description
技术领域technical field
本发明属于新能源发电技术领域,具体涉及一种基于能效最优的水冷型燃料电池电堆低温启动方法。The invention belongs to the technical field of new energy power generation, and in particular relates to a low-temperature start-up method for a water-cooled fuel cell stack based on optimal energy efficiency.
背景技术Background technique
质子交换膜燃料电池(PEMFC)作为清洁能源的一种,具有高效、零污染物排放、长续航、工作温度低等特点,是目前新能源领域的研究热点之一。其工作原理为:氢气在氧化剂的作用下,在阳极分解产生氢质子和电子,氢质子穿过质子交换膜,在阴极与氧气和外电路传输的电子反应,产物为水,对于环境没有污染。As a kind of clean energy, proton exchange membrane fuel cell (PEMFC) has the characteristics of high efficiency, zero pollutant emission, long battery life, and low operating temperature. It is one of the research hotspots in the field of new energy. Its working principle is: under the action of oxidant, hydrogen decomposes at the anode to produce hydrogen protons and electrons. The hydrogen protons pass through the proton exchange membrane and react with oxygen and electrons transmitted by the external circuit at the cathode. The product is water, which has no pollution to the environment.
随着燃料电池在各个领域的广泛应用,对燃料电池低温启动能力的要求越来越高。PEMFC的理想工作温度在75~80℃,整个发电过程是水伴生的电化学反应过程。随着水的不断生成,燃料电池内部将发生水聚集,若环境温度在0℃以下,例如冬天气温较低的城市以及高原地区,产生的水将结冰,阻塞传质通道,影响反应的发生,进而导致燃料电池无法成功启动,且反复的结冰、解冻过程会破坏电池组件的结构,影响PEMFC的耐久性及性能。更为严重的是,此过程将引起体积以及应力的变化,进而导致PEMFC电压骤降,使得反应停止,造成质子交换膜的永久损伤,对材料产生不可逆影响,不仅降低了燃料电池的耐久性,还极大地增加燃料电池的安全隐患。燃料电池低温启动问题是阻碍其发展的主要挑战之一。With the wide application of fuel cells in various fields, the requirements for the low-temperature start-up ability of fuel cells are getting higher and higher. The ideal working temperature of PEMFC is 75-80°C, and the whole power generation process is an electrochemical reaction process accompanied by water. With the continuous generation of water, water will accumulate inside the fuel cell. If the ambient temperature is below 0°C, such as cities and plateau areas with low winter temperatures, the generated water will freeze, blocking the mass transfer channel and affecting the reaction. , which leads to the failure of the fuel cell to start successfully, and the repeated freezing and thawing process will destroy the structure of the battery components and affect the durability and performance of the PEMFC. What's more serious is that this process will cause changes in volume and stress, which will lead to a sudden drop in PEMFC voltage, stop the reaction, cause permanent damage to the proton exchange membrane, and have an irreversible impact on the material, which not only reduces the durability of the fuel cell, It also greatly increases the potential safety hazard of fuel cells. The low-temperature start-up problem of fuel cells is one of the main challenges hindering their development.
根据热源的不同,现有质子交换膜燃料电池低温启动方法主要有自启动和外部辅助加热两种。自启动方法利用电堆自身反应产生的热量来达到提高电堆温度,实现电堆低温启动的目的。这种方法可以避免使用外部设备,不需要添加冗余的装置,节约了使用成本。但各类研究表明,当环境温度在-10℃以下时,自启动是非常困难的,自启动提供的热量十分有限,很难达到快速稳定的效果。外部辅助加热技术是指依靠外界为电堆提供热量,可以稳定地加热电堆,成功实现低温启动。常见的加热方法有:电加热、气体加热以及冷却液加热,这些方法都需要额外的外部设备,会产生较高的能耗。尤其是电加热与冷却液加热,需要大量的热量和加热时间。此外,外部辅助加热技术还容易造成能源浪费。基于以上两种方法的缺陷,需要发明一种既能实现快速的低温启动,又能充分利用能源、达到最大能效的水冷型燃料电池低温启动的装置及控制方法。According to different heat sources, the existing low-temperature starting methods of proton exchange membrane fuel cells mainly include self-starting and external auxiliary heating. The self-starting method uses the heat generated by the self-reaction of the stack to increase the temperature of the stack and realize the purpose of starting the stack at low temperature. This method can avoid the use of external equipment, does not need to add redundant devices, and saves the use cost. However, various studies have shown that when the ambient temperature is below -10°C, self-starting is very difficult, and the heat provided by self-starting is very limited, and it is difficult to achieve a fast and stable effect. The external auxiliary heating technology refers to relying on the outside world to provide heat for the stack, which can stably heat the stack and successfully achieve low-temperature startup. Common heating methods include: electric heating, gas heating, and coolant heating, all of which require additional external equipment and will generate high energy consumption. Especially electric heating and coolant heating require a lot of heat and heating time. In addition, external auxiliary heating technology is also prone to energy waste. Based on the defects of the above two methods, it is necessary to invent a low-temperature start-up device and control method for a water-cooled fuel cell that can not only realize rapid low-temperature start-up, but also make full use of energy and achieve maximum energy efficiency.
发明内容Contents of the invention
针对上述现有技术中存在的问题,本发明提出了一种基于能效最优的水冷型燃料电池电堆低温启动方法,将外部辅助加热技术与电堆自热技术相结合,在保证电堆低温启动成功且不会造成电堆性能衰减的前提下,降低低温启动所需的能耗,实现电堆在低温下快速稳定的高性能输出。Aiming at the problems existing in the above-mentioned prior art, the present invention proposes a water-cooled fuel cell stack low-temperature start-up method based on optimal energy efficiency, which combines external auxiliary heating technology with stack self-heating technology to ensure low temperature of the stack Under the premise of successful start-up and no performance degradation of the stack, the energy consumption required for low-temperature start-up is reduced, and the fast and stable high-performance output of the stack at low temperature is realized.
本发明具体技术方案如下:Concrete technical scheme of the present invention is as follows:
一种基于能效最优的水冷型燃料电池电堆低温启动方法,其特征在于,包括以下步骤:A water-cooled fuel cell stack low-temperature start-up method based on optimal energy efficiency, characterized in that it comprises the following steps:
步骤1:设置水冷型燃料电池电堆自热启动所需的最低温度为Tmin,设置电堆低温启动的最大时间限度为tmax,设置电堆低温启动成功时的电子负载电流密度为Isuc,当电堆电压Vstack不低于最低工作电压Vmin,且电子负载电流密度Istack达到Isuc时,则代表电堆低温启动成功;Step 1: Set the minimum temperature required for the self-heating start of the water-cooled fuel cell stack as T min , set the maximum time limit for the low-temperature start-up of the stack as t max , and set the electronic load current density when the stack starts successfully at low temperature as I suc , when the stack voltage V stack is not lower than the minimum operating voltage V min , and the electronic load current density I stack reaches I suc , it means that the stack starts successfully at low temperature;
步骤2:打开空气进气阀门,将进气压力调节至固定值;Step 2: Open the air intake valve and adjust the intake pressure to a fixed value;
步骤3:开启设置在电堆空气进气端的电加热丝的电源,并将电加热丝功率P调至最大值Pmax,对进入电堆的空气进行加热,电堆开启低温启动;Step 3: Turn on the power supply of the electric heating wire installed at the air intake end of the stack, and adjust the power P of the electric heating wire to the maximum value P max to heat the air entering the stack, and start the stack at low temperature;
步骤4:令开启电加热丝的电源的时刻为初始时刻t0,实时记录电堆低温启动的持续时间t、电堆温度Tstack、电堆电压Vstack以及电子负载电流密度Istack;Step 4: Let the moment when the power supply of the electric heating wire is turned on be the initial time t 0 , and record the duration t of the low-temperature startup of the stack, the stack temperature T stack , the stack voltage V stack and the electronic load current density I stack in real time;
步骤5:对于外辅多约束预测控制器,确定被控变量为电堆温度Tstack,控制变量为电加热丝功率P,约束条件为t≦tmax且Tstack≦Tmin;根据外辅多约束预测控制器的预测结果,实时调整电加热丝功率P,直至电堆温度Tstack达到Tmin,关闭电加热丝的电源;Step 5: For the external auxiliary multi-constraint predictive controller, the controlled variable is determined to be the stack temperature T stack , the control variable is the electric heating wire power P, and the constraints are t≦t max and T stack ≦T min ; according to the external auxiliary multi-constraint Constrain the prediction results of the predictive controller, adjust the power P of the electric heating wire in real time until the stack temperature T stack reaches T min , and turn off the power supply of the electric heating wire;
步骤6:对于自热多约束预测控制器,确定被控变量为电堆温度Tstack,控制变量为电子负载电流密度Istack,约束条件为t≦tmax且Vstack≦Vmin;根据自热多约束预测控制器的预测结果,实时调整电子负载电流密度Istack,直至电子负载电流密度Istack达到Isuc,电堆低温启动成功。Step 6: For the self-heating multi-constraint predictive controller, determine that the controlled variable is the stack temperature T stack , the control variable is the electronic load current density I stack , and the constraints are t≦t max and V stack ≦V min ; according to the self-heating According to the prediction result of the multi-constraint predictive controller, the electronic load current density I stack is adjusted in real time until the electronic load current density I stack reaches I suc , and the stack starts successfully at low temperature.
进一步地,步骤1中依据电堆结构和环境温度设置Tmin和Isuc。Further, in step 1, T min and I suc are set according to the stack structure and ambient temperature.
进一步地,步骤3中Pmax为5~10KW。Further, in step 3, P max is 5-10KW.
进一步地,所述外辅多约束预测控制器和自热多约束预测控制器为具有纯滞后对象的控制器,采用的算法为基于二次规划的约束优化算法。Further, the external auxiliary multi-constraint predictive controller and the self-heating multi-constraint predictive controller are controllers with pure hysteresis objects, and the algorithm adopted is a constrained optimization algorithm based on quadratic programming.
本发明的有益效果为:The beneficial effects of the present invention are:
1、本发明提出了一种基于能效最优的水冷型燃料电池电堆低温启动方法,先利用外辅多约束预测控制器调节电加热丝功率,对电堆进行预热,当电堆达到一定温度时,通过自热多约束预测控制器调节电子负载电流密度,实现电堆自加热,进而完成电堆低温启动;1. The present invention proposes a water-cooled fuel cell stack low-temperature start-up method based on optimal energy efficiency. First, the external auxiliary multi-constraint predictive controller is used to adjust the power of the electric heating wire to preheat the stack. When the stack reaches a certain When the temperature is high, the current density of the electronic load is adjusted by the self-heating multi-constraint predictive controller to realize the self-heating of the stack, and then complete the low-temperature startup of the stack;
2、本发明将电堆低温启动时间控制在安全范围内,避免因低温启动过程过长而破坏电堆的性能,安全可靠,同时能量利用最大化,大大降低成本,节约资源,实现快速稳定、能效最优的水冷型燃料电池低温启动控制;2. The present invention controls the low-temperature start-up time of the stack within a safe range, avoids damage to the performance of the stack due to too long low-temperature start-up process, is safe and reliable, and at the same time maximizes energy utilization, greatly reduces costs, saves resources, and achieves fast, stable, Water-cooled fuel cell low-temperature start-up control with optimal energy efficiency;
3、本发明提供的控制方法可以通过编程实现全自动控制,实施过程简单高效,有利于跟具体的工程应用相结合,便于实际地解决水冷燃料电池在工程应用中的问题。3. The control method provided by the present invention can realize fully automatic control through programming, and the implementation process is simple and efficient, which is beneficial to combine with specific engineering applications, and is convenient for practically solving the problems of water-cooled fuel cells in engineering applications.
附图说明Description of drawings
图1为本发明实施例1提出的基于能效最优的水冷型燃料电池电堆低温启动方法的流程图;Fig. 1 is a flow chart of a low-temperature start-up method for a water-cooled fuel cell stack based on optimal energy efficiency proposed in Embodiment 1 of the present invention;
图2为本发明实施例1中外部辅热过程的燃料电池系统工作示意图;Fig. 2 is a working schematic diagram of the fuel cell system in the external auxiliary heating process in Example 1 of the present invention;
图3为本发明实施例1中电堆自热过程的燃料电池系统工作示意图;Fig. 3 is a working schematic diagram of the fuel cell system in the stack self-heating process in Embodiment 1 of the present invention;
图4为本发明实施例1中外部辅热过程的燃料电池电堆温度控制方法原理图;Fig. 4 is a schematic diagram of the fuel cell stack temperature control method in the external auxiliary heating process in Example 1 of the present invention;
图5为本发明实施例1中电堆自热过程的燃料电池电堆温度控制方法原理图;5 is a schematic diagram of a fuel cell stack temperature control method in the self-heating process of the stack in Embodiment 1 of the present invention;
图6为本发明实施例1中启动温度为-30℃时的外辅多约束预测控制器的控制结果;Fig. 6 is the control result of the external auxiliary multi-constraint predictive controller when the start-up temperature is -30°C in Example 1 of the present invention;
图7为本发明实施例1中启动温度为-30℃时的自热多约束预测控制器的控制结果。Fig. 7 is the control result of the self-heating multi-constraint predictive controller when the start-up temperature is -30°C in Example 1 of the present invention.
具体实施方式detailed description
为使本发明的目的、技术方案和优点更加清晰,结合以下具体实施例,并参照附图,对本发明做进一步的说明。In order to make the purpose, technical solution and advantages of the present invention clearer, the present invention will be further described in conjunction with the following specific embodiments and with reference to the accompanying drawings.
下述非限制性实施例可以使本领域的普通技术人员更全面的理解本发明,但不以任何方式限制本发明。The following non-limiting examples can enable those skilled in the art to understand the present invention more fully, but do not limit the present invention in any way.
实施例1Example 1
本实施例提出了一种基于能效最优的水冷型燃料电池电堆低温启动方法,基于如图2和图3所示的燃料电池系统实现,包括水冷型燃料电池电堆,电子负载,用于测量电堆温度的温度传感器,用于测量电堆电压的电压测量仪,放置在电堆空气进气端的电加热丝,为电加热丝供电的电源,外辅多约束预测控制器,以及自热多约束预测控制器。This embodiment proposes a water-cooled fuel cell stack low-temperature start-up method based on optimal energy efficiency, which is implemented based on the fuel cell system shown in Figure 2 and Figure 3, including water-cooled fuel cell stacks, electronic loads, and A temperature sensor for measuring the stack temperature, a voltage measuring instrument for measuring the stack voltage, an electric heating wire placed at the air intake end of the stack, a power supply for the electric heating wire, an external auxiliary multi-constraint predictive controller, and self-heating Multiple Constraint Predictive Controller.
本实施例所述水冷型燃料电池电堆低温启动方法的流程如图1所示,具体包括以下步骤:The flow chart of the method for starting the water-cooled fuel cell stack at low temperature in this embodiment is shown in Figure 1, which specifically includes the following steps:
步骤1:设置水冷型燃料电池电堆自热启动所需的最低温度为Tmin=-10℃,设置电堆低温启动的最大时间限度为tmax=90s,设置电堆低温启动成功时的电子负载电流密度为Isuc=0.6A/cm2,当电堆电压Vstack不低于最低工作电压Vmin=0.5V,且电子负载电流密度Istack达到Isuc时,则代表电堆低温启动成功;Step 1: Set the minimum temperature required for the self-heating start of the water-cooled fuel cell stack as T min = -10°C, set the maximum time limit for the low-temperature start-up of the stack as t max = 90s, and set the electronic temperature when the stack starts successfully at low temperature The load current density is I suc = 0.6A/cm 2 , when the stack voltage V stack is not lower than the minimum operating voltage V min = 0.5V, and the electronic load current density I stack reaches I suc , it means that the stack starts successfully at low temperature ;
步骤2:打开空气进气阀门,将进气压力调节至固定值20KPa;Step 2: Open the air intake valve and adjust the intake pressure to a fixed value of 20KPa;
步骤3:进行燃料电池系统的外部辅热过程,如图2所示,具体为:Step 3: Carry out the external auxiliary heating process of the fuel cell system, as shown in Figure 2, specifically:
步骤3.1:开启设置在电堆空气进气端的电加热丝的电源,并将电加热丝功率P调至最大值Pmax=5KW,对进入电堆的空气进行加热,电堆低温启动过程开始;Step 3.1: Turn on the power supply of the electric heating wire installed at the air intake end of the stack, and adjust the power P of the electric heating wire to the maximum value P max = 5KW to heat the air entering the stack, and the low-temperature start-up process of the stack begins;
步骤3.2:令开启电加热丝的电源的时刻为初始时刻t0=0,实时记录电堆低温启动的持续时间t、电堆温度Tstack、电堆电压Vstack以及电子负载电流密度Istack;Step 3.2: Let the moment of turning on the power supply of the electric heating wire be the initial moment t 0 =0, and record the duration t of the low-temperature start-up of the stack, the stack temperature T stack , the stack voltage V stack and the electronic load current density I stack in real time;
步骤3.3:如图4所示,对于外辅多约束预测控制器,确定被控变量为电堆温度Tstack,控制变量为电加热丝功率P,约束条件为t≦tmax且Tstack≦Tmin;Step 3.3: As shown in Figure 4, for the external auxiliary multi-constraint predictive controller, the controlled variable is determined to be the stack temperature T stack , the controlled variable is the electric heating wire power P, and the constraint conditions are t≦t max and T stack ≦T min ;
将上一时刻t、电堆温度Tstack以及电加热丝功率P作为外辅多约束预测控制器的输入,预测下一时刻t+1的电堆温度以及电加热丝功率,然后根据外辅多约束预测控制器的预测结果,实时调整电加热丝功率P;Taking the last time t, the stack temperature T stack and the electric heating wire power P as the input of the external auxiliary multi-constraint predictive controller, predict the next time t+1 stack temperature and electric heating wire power, and then according to the external auxiliary multi-constraint Constrain the prediction results of the predictive controller, and adjust the electric heating wire power P in real time;
选取某次实验的数据做解释说明:当电堆温度Tstack为-20℃,此时的电加热丝功率P为4.02KW,那么将此时的电堆温度Tstack和电加热丝功率P作为外辅多约束预测控制器的输入,外辅多约束预测控制器计算可得下一时刻的加热丝功率应为3.84KW;Select the data of a certain experiment for explanation: when the stack temperature T stack is -20°C, the electric heating wire power P at this time is 4.02KW, then the electric stack temperature T stack and the electric heating wire power P at this time are taken as The input of the external auxiliary multi-constraint predictive controller, the external auxiliary multi-constraint predictive controller calculates that the power of the heating wire at the next moment should be 3.84KW;
以此类推,直至电堆温度Tstack达到Tmin,得到如图6所示的外辅多约束预测控制器的控制结果(即控制轨迹),关闭电加热丝的电源;By analogy, until the stack temperature T stack reaches T min , the control result (that is, the control trajectory) of the external auxiliary multi-constraint predictive controller shown in Figure 6 is obtained, and the power supply of the electric heating wire is turned off;
步骤4:进行燃料电池系统的电堆自热过程,如图3所示,具体为:Step 4: Carry out the stack self-heating process of the fuel cell system, as shown in Figure 3, specifically:
如图5所示,对于自热多约束预测控制器,确定被控变量为电堆温度Tstack,控制变量为电子负载电流密度Istack,约束条件为t≦tmax且Vstack≦Vmin;As shown in Figure 5, for the self-heating multi-constraint predictive controller, the controlled variable is determined to be the stack temperature T stack , the control variable is the electronic load current density I stack , and the constraints are t≦t max and V stack ≦V min ;
将上一时刻t、电堆电压Vstack以及电子负载电流密度Istack作为自热多约束预测控制器的输入,预测下一时刻t+1的电堆温度以及电子负载电流密度,然后根据自热多约束预测控制器的预测结果,实时调整电子负载电流密度Istack;Taking the last time t, the stack voltage V stack and the electronic load current density I stack as the input of the self-heating multi-constraint predictive controller, predict the stack temperature and the electronic load current density at the next time t+1, and then according to the self-heating The prediction result of the multi-constraint predictive controller adjusts the electronic load current density I stack in real time;
选取某次实验的数据做解释说明:当负载电流密度为0.24A/cm2时,此时的电堆电压Vstack为0.857V,符合小于Vmin的要求,将此时的负载电流密度以及电堆电压作为自热多约束预测控制器输入,自热多约束预测控制器计算可得下一时刻的负载电流密度应为0.31A/cm2;The data of an experiment is selected for explanation: when the load current density is 0.24A/cm 2 , the stack voltage V stack at this time is 0.857V, which meets the requirement of being less than V min . The stack voltage is taken as the input of the self-heating multi-constraint predictive controller, and the self-heating multi-constraint predictive controller calculates that the load current density at the next moment should be 0.31A/cm 2 ;
以此类推,直至电子负载电流密度Istack达到Isuc,得到如图7所示的自热多约束预测控制器的控制结果,电堆低温启动成功。By analogy, until the electronic load current density I stack reaches I suc , the control result of the self-heating multi-constraint predictive controller shown in Figure 7 is obtained, and the stack starts successfully at low temperature.
最后说明的是,以上实施例仅用以说明本发明的技术方案而非限制,尽管参照实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本技术方案的宗旨和范围,其均应涵盖在本发明的权利要求范围当中。Finally, it is noted that the above embodiments are only used to illustrate the technical solutions of the present invention without limitation. Although the present invention has been described in detail with reference to the embodiments, those of ordinary skill in the art should understand that the technical solutions of the present invention can be modified or Equivalent replacements without departing from the spirit and scope of the technical solution shall be covered by the scope of the claims of the present invention.
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