CN115074776A - Intelligent adaptive control system and method for electrolysis of water for hydrogen production adapting to wide power fluctuations - Google Patents
Intelligent adaptive control system and method for electrolysis of water for hydrogen production adapting to wide power fluctuations Download PDFInfo
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 169
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 169
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 142
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 50
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 36
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- 238000005868 electrolysis reaction Methods 0.000 title claims description 27
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- 239000001301 oxygen Substances 0.000 claims description 110
- 229910052760 oxygen Inorganic materials 0.000 claims description 110
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 108
- 239000007788 liquid Substances 0.000 claims description 34
- 150000002431 hydrogen Chemical class 0.000 claims description 27
- 230000001105 regulatory effect Effects 0.000 claims description 12
- 238000003860 storage Methods 0.000 claims description 9
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Abstract
本发明涉及适应宽功率波动的电解水制氢智能自适应控制系统与方法,系统包括:专家经验知识库模块:用于获取电解槽在满足边界条件限制下的期望输出参数;回馈补偿模块:用于检测电解槽运行后的输出参数与边界条件之间的偏差值,输出专家经验补偿值;电解水制氢模块:用于根据专家经验补偿值与专家经验知识库的输出值控制电解槽在输入功率存在波动情况下的稳定运行。本发明可以在适应宽功率波动的前提下通过各个模块的配合,得到制氢系统参数给定值,既可以使电解水制氢模块在可再生能源波动的影响下安全稳定运行且制氢效率提高,制出来的氢气为高纯度。
The invention relates to an intelligent self-adaptive control system and method for electrolyzing water for hydrogen production that can adapt to wide power fluctuations. The system includes: an expert experience knowledge base module: used to obtain expected output parameters of an electrolytic cell under the limit of boundary conditions; a feedback compensation module: used It is used to detect the deviation value between the output parameters and boundary conditions of the electrolyzer after operation, and output the expert experience compensation value; electrolyzed water hydrogen production module: used to control the input value of the electrolyzer according to the expert experience compensation value and the output value of the expert experience knowledge base. Stable operation in the presence of power fluctuations. The present invention can obtain the given value of the parameters of the hydrogen production system through the cooperation of various modules under the premise of adapting to wide power fluctuations, so that the electrolyzed water hydrogen production module can operate safely and stably under the influence of the fluctuation of renewable energy, and the hydrogen production efficiency can be improved , the hydrogen produced is of high purity.
Description
技术领域technical field
本发明涉及电解水制氢技术领域,特别是涉及适应宽功率波动的电解水制氢智能自适应控制系统与方法。The invention relates to the technical field of electrolysis of water for hydrogen production, in particular to an intelligent adaptive control system and method for electrolysis of water for hydrogen production which can adapt to wide power fluctuations.
背景技术Background technique
氢能源作为清洁低碳能源,具有清洁性、储存性和高能量载体等各种优势被认为是21世纪最有前途的二次能源,也是推动能源结构变革、实现“双碳”目标的关键路径之一。但目前化石能源制氢是主流的制氢方式,制出来的氢气纯度较低,为了减少大量使用化石燃料对人体健康和环境的危害,国家鼓励将可再生能源进行制氢,这样制出来的氢为绿氢,且纯度高达99.95%以上,绿氢才是未来主流。 As a clean and low-carbon energy, hydrogen energy has various advantages such as cleanliness, storage and high energy carrier, and is considered to be the most promising secondary energy in the 21st century. one. However, at present, hydrogen production from fossil energy is the mainstream method of hydrogen production, and the purity of the hydrogen produced is low. In order to reduce the harm to human health and the environment caused by the large-scale use of fossil fuels, the state encourages the production of hydrogen from renewable energy. It is green hydrogen with a purity of more than 99.95%. Green hydrogen will be the mainstream in the future.
其中在制氢过程中,碱性水电解是工业生产绿色氢气最有前景的方法,但是由于可再生能源如风、光等发电具有不确定性,使得电解槽的给定功率会存在较大波动性,则可能会导致电解槽系统中的一些关键参数超出安全边界条件,进而产生严重后果。例如某一时刻电解槽系统输入功率出现大范围波动,会使氧气洗涤器中的氧中氢含量不在安全范围(2%以下)内,为了避免产生爆炸危险,系统会自动安全报警并使电解槽系统停机,进一步影响了制氢效率和系统的安全。因此,研究适应宽功率波动的电解槽系统控制方法,在系统安全运行的前提下,保证电解槽连续稳定运行并最大限度的提高产氢量,是本申请的重要的意义所在。Among them, in the process of hydrogen production, alkaline water electrolysis is the most promising method for industrial production of green hydrogen. However, due to the uncertainty of renewable energy such as wind and solar power generation, the given power of the electrolyzer will fluctuate greatly. However, it may cause some key parameters in the electrolyzer system to exceed the safe boundary conditions, resulting in serious consequences. For example, if the input power of the electrolyzer system fluctuates in a large range at a certain time, the hydrogen content in the oxygen in the oxygen scrubber will not be within the safe range (below 2%). In order to avoid the danger of explosion, the system will automatically alarm and make the electrolyzer The shutdown of the system further affects the hydrogen production efficiency and the safety of the system. Therefore, it is of great significance of the present application to study the control method of the electrolyzer system adapting to wide power fluctuation, to ensure the continuous and stable operation of the electrolyzer and maximize the hydrogen production under the premise of the safe operation of the system.
发明内容SUMMARY OF THE INVENTION
本发明的目的是提供适应宽功率波动的电解水制氢智能自适应控制系统与方法,通过专家经验知识库模型,回馈补偿模块和电解水制氢模块之间的相互合作,使得电解槽可以适应不同的功率波动,保证电解槽能够安全稳定的运行,提高电解槽的制氢效率。The purpose of the present invention is to provide an intelligent self-adaptive control system and method for electrolyzed water for hydrogen production that can adapt to wide power fluctuations. Through the expert experience knowledge base model, the mutual cooperation between the feedback compensation module and the electrolyzed water hydrogen production module enables the electrolyzer to adapt to the Different power fluctuations ensure the safe and stable operation of the electrolyzer and improve the hydrogen production efficiency of the electrolyzer.
为实现上述目的,本发明提供了如下方案:For achieving the above object, the present invention provides the following scheme:
适应宽功率波动的电解水制氢智能自适应控制系统,包括:An intelligent adaptive control system for electrolysis of water for hydrogen production that adapts to wide power fluctuations, including:
专家经验知识库模块:用于获取电解槽在满足边界条件限制下的期望输出参数,其中所述边界条件用于限制系统参数,保证系统的安全运行,所述期望输出参数用于使系统运行时的参数满足设置的边界条件;Expert experience knowledge base module: used to obtain the expected output parameters of the electrolyzer under the constraints of the boundary conditions, where the boundary conditions are used to limit the system parameters and ensure the safe operation of the system, and the expected output parameters are used to make the system run The parameters satisfy the set boundary conditions;
回馈补偿模块:用于检测所述电解槽运行后的输出参数与所述边界条件之间的偏差值,输出专家经验补偿值;Feedback compensation module: used to detect the deviation value between the output parameters of the electrolyzer after operation and the boundary conditions, and output the expert experience compensation value;
电解水制氢模块:用于根据所述专家经验补偿值与专家经验知识库的输出值控制所述电解槽在输入功率存在波动情况下的稳定运行。Water electrolysis hydrogen production module: used to control the stable operation of the electrolytic cell under the condition of fluctuations in input power according to the expert experience compensation value and the output value of the expert experience knowledge base.
优选地,所述专家经验知识库模块,包括:Preferably, the expert experience knowledge base module includes:
专家经验知识库模型:用于根据当前所述电解槽输入的功率,以及当前所述电解槽的运行实测参数Yk,在所述边界条件的限制下,获取所述电解槽在满足所述边界条件的限制下的期望输出参数。Expert experience knowledge base model: used to obtain the current input power of the electrolytic cell and the current measured operating parameter Y k of the electrolytic cell, under the restriction of the boundary conditions, to obtain the electrolytic cell that satisfies the boundary The expected output parameters under the constraints of the condition.
优选地,所述电解槽的运行实测参数Yk包括:系统压力、碱液流量、电解槽温度、氧气分离器和氢气分离器的液位差、氧气洗涤器中的氧中氢含量、氢气洗涤器中的氢中氧含量。Preferably, the measured parameters Y k of the electrolyzer include: system pressure, lye flow rate, temperature of the electrolyzer, liquid level difference between the oxygen separator and the hydrogen separator, the hydrogen content in the oxygen in the oxygen scrubber, the hydrogen scrubber Oxygen content of hydrogen in the vessel.
优选地,所述专家经验知识库模块中还包括查询与匹配单元,所述查询与匹配单元用于基于多属性相似度算法,计算通过当前所述电解槽运行特征参数在符合所述边界条件里的知识库中对专家经验知识进行查询和匹配,筛选出所述知识库中与当前所述电解槽工况最为接近的期望输出值。Preferably, the expert experience knowledge base module further includes a query and matching unit, and the query and matching unit is configured to calculate, based on a multi-attribute similarity algorithm, the current operating characteristic parameters of the electrolytic cell within the boundary conditions that meet the boundary conditions. Query and match the expert's experience knowledge in the knowledge base, and filter out the expected output value in the knowledge base that is closest to the current working condition of the electrolytic cell.
优选地,所述多属性相似度算法包括最邻近算法、欧氏距离和结构相似度,基于所述多属性相似度算法获得所述电解槽当前运行参数与所述专家经验知识的整体相似度,基于所述相似度进行查询和匹配。Preferably, the multi-attribute similarity algorithm includes a nearest neighbor algorithm, Euclidean distance and structural similarity, and based on the multi-attribute similarity algorithm, the overall similarity between the current operating parameters of the electrolytic cell and the expert experience knowledge is obtained, Queries and matches are performed based on the similarity.
优选地,所述专家经验知识库模块中还包括评价与修正单元和存储与添加单元,所述评价与修正单元用于对所述专家经验知识库中专家经验知识重用结果进行评价与修正,根据所述电解槽运行时的重要参数是否满足所述边界条件来判断是否对所述专家经验知识进行修正,若当前所述重要参数超出边界条件则需要对专家经验知识进行修正,若所述重要参数都在所述边界条件内,则不需要对专家经验知识进行修正;其中所述重要参数包括氧中氢含量,氢中氧含量,液位差以及碱液温度;所述存储与添加单元用于加入新的专家经验知识。Preferably, the expert experience knowledge base module further includes an evaluation and correction unit and a storage and addition unit, and the evaluation and correction unit is used to evaluate and correct the reuse result of the expert experience knowledge in the expert experience knowledge base, according to Whether the important parameters during the operation of the electrolytic cell meet the boundary conditions is used to judge whether to correct the expert experience knowledge. If the current important parameters exceed the boundary conditions, the expert experience knowledge needs to be corrected. If the important parameters are all within the boundary conditions, so there is no need to revise the expert experience and knowledge; wherein the important parameters include the hydrogen content in oxygen, the oxygen content in hydrogen, the liquid level difference and the temperature of the lye; the storage and addition unit is used for Add new expert experience knowledge.
优选地,所述回馈补偿模块包括:Preferably, the feedback compensation module includes:
专家规则建立单元:用于根据所述电解槽运行后输出的所述重要参数与边界值之间的偏差设置规则,专家根据经验和规律,对每种偏差给出参数补偿的相关系数;其中,所述规则包括:电解槽运行中的氧中氢含量与边界值阈值之间的误差、电解槽运行中的氢中氧含量与边界值阈值之间的误差、电解槽运行中的液位差与边界值阈值之间的误差和电解槽运行中的碱液温度和边界值阈值之间的误差;Expert rule establishment unit: used to set rules according to the deviation between the important parameters outputted after the electrolyzer runs and the boundary value, and experts give the correlation coefficient of parameter compensation for each deviation according to experience and rules; wherein, The rules include: the error between the hydrogen content in the oxygen in the electrolytic cell operation and the boundary value threshold, the error between the oxygen content in the hydrogen in the electrolytic cell operation and the boundary value threshold, the liquid level difference in the electrolytic cell operation and the boundary value threshold value. The error between the boundary value thresholds and the error between the lye temperature and the boundary value thresholds in the operation of the electrolyser;
推理机单元:用于根据所述电解槽运行中输出的重要参数与所述边界值之间的差值,通过专家经验规则采用穷尽式逐项搜索算法推理出相应的专家经验补偿值,并输出所述专家经验补偿值。Inference engine unit: used to infer the corresponding expert experience compensation value by using an exhaustive item-by-item search algorithm through expert empirical rules according to the difference between the important parameters outputted during the operation of the electrolytic cell and the boundary value, and output The expert experience compensation value.
优选地,所述电解水制氢模块用于通过模糊规则和神经网络结合对所述电解槽中的压力调节阀以及气动调节阀进行瞬态PID控制,保证所述电解槽当前时刻的压力、氧分离器和氢分离器的液位以及碱液温度和流量进行响应趋于重要参数的给定值。Preferably, the water electrolysis hydrogen production module is used to perform transient PID control on the pressure regulating valve and the pneumatic regulating valve in the electrolytic cell through the combination of fuzzy rules and neural network, so as to ensure the pressure and oxygen of the electrolytic cell at the current moment. Separator and hydrogen separator levels, as well as lye temperature and flow, respond to given values of important parameters.
适应宽功率波动的电解水制氢智能自适应控制方法,包括:An intelligent adaptive control method for hydrogen production from electrolyzed water that adapts to wide power fluctuations, including:
构建专家经验知识库模型,根据当前电解槽的输入功率与实测参数,获得所述电解槽系统在满足边界条件限制下的期望输出参数,其中所述边界条件包括:氧中氢含量、氢中氧含量、碱液流量、碱液温度和氧分离器和氢分离器液位差,所述期望输出参数包括系统压力给定值、碱液温度给定值和碱液流量给定值;Build an expert experience knowledge base model, according to the current input power and measured parameters of the electrolyzer, obtain the expected output parameters of the electrolyzer system under the constraints of boundary conditions, wherein the boundary conditions include: hydrogen content in oxygen, oxygen in hydrogen Content, lye flow, lye temperature and liquid level difference between oxygen separator and hydrogen separator, and the expected output parameters include a given value of system pressure, a given value of lye temperature and a given value of lye flow;
基于所述期望输出参数运行所述电解槽系统,通过回馈补偿模型检测所述电解槽系统运行后的输出参数与所述边界条件之间的偏差值,输出专家经验补偿值;The electrolytic cell system is operated based on the expected output parameters, the deviation value between the output parameters of the electrolytic cell system after operation and the boundary conditions is detected by a feedback compensation model, and an expert experience compensation value is output;
根据所述专家经验补偿值与期望输出参数,通过模糊规则与神经网络结合控制所述电解槽中的压力调节阀以及气动调节阀进行瞬态PID控制,同时每隔相同时间将输出边界重要参数检测值到回馈补偿模型和专家经验知识库模型中进行监测及修正。According to the expert experience compensation value and expected output parameters, the pressure regulating valve and the pneumatic regulating valve in the electrolytic cell are controlled by fuzzy rules and neural network for transient PID control, and the important parameters of the output boundary are detected at the same time. The value is monitored and corrected in the feedback compensation model and the expert experience knowledge base model.
本发明的有益效果为:The beneficial effects of the present invention are:
本发明可以在适应可再生能源发电不确定性导致碱性电解槽宽功率波动的基础上,通过智能控制方法自适应的控制电解槽给定参数 (系统压力、碱液流量、碱液温度)使电解槽系统的重要参数(氧中氢含量等)保持在安全范围内,达到电解槽系统在保证安全稳定运行的条件下,有效的提高了电解槽的制氢效率和制出氢气纯度。The present invention can adaptively control the given parameters (system pressure, lye flow, lye temperature) of the electrolyzer through the intelligent control method on the basis of adapting to the wide power fluctuation of the alkaline electrolyzer caused by the uncertainty of renewable energy power generation. The important parameters of the electrolyzer system (hydrogen content in oxygen, etc.) are kept within a safe range, so that the electrolyzer system can effectively improve the hydrogen production efficiency and the purity of hydrogen produced under the condition of ensuring safe and stable operation of the electrolyzer system.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动性的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the accompanying drawings required in the embodiments will be briefly introduced below. Obviously, the drawings in the following description are only some of the present invention. In the embodiments, for those of ordinary skill in the art, other drawings can also be obtained according to these drawings without creative labor.
图1为本发明实施例的适应宽功率波动的电解水制氢智能自适应控制系统的模块结构示意图;FIG. 1 is a schematic structural diagram of a module of an intelligent self-adaptive control system for electrolysis of water for hydrogen production that adapts to wide power fluctuations according to an embodiment of the present invention;
图2为本发明实施例的不同电解槽输入功率范围和不同系统压力下的氧中氢含量折线图;2 is a broken line diagram of hydrogen content in oxygen under different electrolyzer input power ranges and different system pressures according to the embodiment of the present invention;
图3为本发明实施例的不同功率范围和不同系统压力下的氧中氢含量安全区域示意图;3 is a schematic diagram of a safe area of hydrogen content in oxygen under different power ranges and different system pressures according to an embodiment of the present invention;
图4为本发明实施例的不同功率范围和不同系统压力下的氢中氧含量折线图;4 is a broken line diagram of oxygen content in hydrogen under different power ranges and different system pressures according to an embodiment of the present invention;
图5为本发明实施例的不同功率范围和不同系统压力下的分离器液位差示意图;5 is a schematic diagram of the liquid level difference of the separator under different power ranges and different system pressures according to an embodiment of the present invention;
图6为本发明实施例的不同功率压力的能耗与能效示意图;6 is a schematic diagram of energy consumption and energy efficiency of different power pressures according to an embodiment of the present invention;
图7为本发明实施例的适应宽功率波动的电解水制氢智能自适应控制方法流程图;FIG. 7 is a flowchart of an intelligent adaptive control method for electrolysis of water for hydrogen production that adapts to wide power fluctuations according to an embodiment of the present invention;
图8为本发明实施例的专家经验知识库模块工作流程示意图。FIG. 8 is a schematic diagram of a workflow of an expert experience knowledge base module according to an embodiment of the present invention.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, but not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
为使本发明的上述目的、特征和优点能够更加明显易懂,下面结合附图和具体实施方式对本发明作进一步详细的说明。In order to make the above objects, features and advantages of the present invention more clearly understood, the present invention will be described in further detail below with reference to the accompanying drawings and specific embodiments.
可再生能源发电后,通过直流微网向碱性电解槽输出功率,提供给电解槽的功率波动比较大,可能会导致制氢系统的重要参数超过安全运行边界条件。例如:After the renewable energy is generated, the power is output to the alkaline electrolyzer through the DC microgrid, and the power supplied to the electrolyzer is relatively fluctuating, which may cause the important parameters of the hydrogen production system to exceed the safe operation boundary conditions. E.g:
1)氧气洗涤器中的氧中氢含量超过2%,一旦超过2%,就会有爆炸危险。另外碱性电解水制氢的氢气要求高纯度,限制氢气洗涤器中的氢中氧含量不能超过0.5%;1) The hydrogen content in the oxygen in the oxygen scrubber exceeds 2%, and once it exceeds 2%, there is a danger of explosion. In addition, the hydrogen produced by alkaline electrolysis of water requires high purity, and the oxygen content in the hydrogen in the hydrogen scrubber is restricted to not exceed 0.5%;
2)氧气分离器的液位和氢气分离器的液位如果偏差较大,可能会导致碱液进入洗涤器,经洗涤器由放空口喷出,如果有人从防空口下经过,可能发生碱烧伤事故,另外若一侧液位过低,此时分离器中的气体和碱液有可能同时进入循环泵中,使碱液循环量产生大幅波动,甚至停止转动,如果碱液停止循环,液位偏差有可能继续增大,则一侧分离器中的气体会进入另一侧分离器中,在分离其中发生氢氧混合现象,极易在分离器中爆炸,发生严重安全事故,因此设置氧气分离和氢气分离器的液位差不能超过5cm;2) If there is a large deviation between the liquid level of the oxygen separator and the liquid level of the hydrogen separator, it may cause the lye to enter the scrubber and be ejected from the vent through the scrubber. If someone passes under the air defense port, alkali burns may occur. In addition, if the liquid level on one side is too low, the gas and lye in the separator may enter the circulating pump at the same time, causing the circulating amount of lye to fluctuate greatly, or even stop rotating. The deviation may continue to increase, and the gas in the separator on one side will enter the separator on the other side, and the hydrogen-oxygen mixing phenomenon will occur in the separation, which will easily explode in the separator and cause serious safety accidents. Therefore, oxygen separation is set up. The liquid level difference with the hydrogen separator cannot exceed 5cm;
3)在碱性电解槽运行过程中,主要通过碱液来控制槽体温度,其中碱液温度要求控制在65℃左右,上下波动要小于1.1℃,碱液流量越大,氢槽温和氧槽温的温度越低,由于电解槽的阴极和阳极之间的隔膜对温度由一定要求,电解槽运行时氢槽温和氧槽温应小于85℃,如果碱液流量过低,导致分离器的温度超过边界温度,会使电解槽的阴极和阳极之间的隔膜破损,使得两侧的氢气和氧气混合,造成严重后果。3) During the operation of the alkaline electrolytic cell, the temperature of the cell body is mainly controlled by the lye solution. The temperature of the lye solution is required to be controlled at about 65 °C, and the fluctuation should be less than 1.1 °C. The lower the temperature is, because the diaphragm between the cathode and the anode of the electrolytic cell has certain requirements on the temperature, the temperature of the hydrogen tank and oxygen tank should be less than 85 ℃ when the electrolytic cell is running. If the lye flow rate is too low, the temperature of the separator will be caused. Exceeding the boundary temperature will damage the diaphragm between the cathode and anode of the electrolytic cell, causing hydrogen and oxygen on both sides to mix, causing serious consequences.
4)另外,碱液流量也会影响氢气和氧气的纯度,如果碱液流量过大,会使分离器中电解产生的气液混合物携带的杂质气越多,导致氧气分离器和氢气分离器中的氧气和氢气的纯度下降。本实施例设置碱液流量范围在3.0-4.5m3/h内。4) In addition, the flow of lye will also affect the purity of hydrogen and oxygen. If the flow of lye is too large, the gas-liquid mixture produced by electrolysis in the separator will carry more impurity gas, resulting in the oxygen separator and hydrogen separator. The purity of oxygen and hydrogen decreased. In this embodiment, the lye flow rate range is set within 3.0-4.5 m 3 /h.
此外,上述中的氧中氢含量、氢中氧含量、氧气分离器与氢气分离器之间的液位差、碱液流量、碱液温度如果超出了边界条件不仅会对系统安全造成严重影响还会导致制氢效率和产氢量降低。In addition, if the above-mentioned hydrogen content in oxygen, oxygen content in hydrogen, liquid level difference between oxygen separator and hydrogen separator, lye flow rate, and lye temperature exceed the boundary conditions, it will not only have a serious impact on system safety but also It will lead to the reduction of hydrogen production efficiency and hydrogen production.
参照附图1,本实施例提供适应宽功率波动的电解水制氢智能自适应控制系统,包括:Referring to FIG. 1, the present embodiment provides an intelligent adaptive control system for electrolysis of water for hydrogen production that adapts to wide power fluctuations, including:
专家经验知识库模块:用于获取电解槽在满足边界条件限制下的期望输出参数,其中所述边界条件包括:氧中氢含量、氢中氧含量、碱液流量、碱液温度和氧分离器和氢分离器液位差,所述期望输出参数包括系统压力给定值、碱液浓度给定值和碱液流量给定值;Expert experience knowledge base module: used to obtain the expected output parameters of the electrolyzer under the constraints of the boundary conditions, wherein the boundary conditions include: hydrogen content in oxygen, oxygen content in hydrogen, lye flow, lye temperature and oxygen separator and the liquid level difference of the hydrogen separator, the expected output parameters include a given value of system pressure, a given value of lye concentration and a given value of lye flow;
回馈补偿模块:用于检测所述电解槽运行后的输出参数与所述边界条件之间的偏差值,输出专家经验补偿值;Feedback compensation module: used to detect the deviation value between the output parameters of the electrolyzer after operation and the boundary conditions, and output the expert experience compensation value;
电解水制氢模块:用于根据所述专家经验补偿值与专家经验知识库的输出值控制所述电解槽在输入功率存在波动情况下的稳定运行。Water electrolysis hydrogen production module: used to control the stable operation of the electrolytic cell under the condition of fluctuations in input power according to the expert experience compensation value and the output value of the expert experience knowledge base.
(1)专家经验知识库模型(1) Expert Experience Knowledge Base Model
专家经验知识库模型是根据当前电解槽系统输入的功率,综合考虑当前电解槽系统的当前运行实测参数Yk,在边界条件Bk的限制下,根据专家经验知识库模型,协调给出电解槽系统在满足边界条件的限制下的闭环给定值Zk。The expert experience knowledge base model is based on the input power of the current electrolytic cell system, and comprehensively considers the current measured parameters Y k of the current electrolytic cell system. Under the limit of the boundary condition B k , according to the expert experience knowledge base model, coordinate the given electrolytic cell The closed-loop given value Z k of the system under the constraints that satisfy the boundary conditions.
其中输入到专家经验知识库的电解槽系统的各个实测参数(Yk) 分别为系统压力、碱液流量、电解槽温度、氧气分离器和氢气分离器的液位差、氧气洗涤器中的氧中氢含量、氢气洗涤器中的氢中氧含量。在边界条件的约束下根据知识库推理和数学模型相结合的方法得出电解槽系统的期望输出参数,分别为系统压力给定值、碱液温度给定值、碱液流量给定值。The measured parameters (Y k ) of the electrolyzer system entered into the expert experience knowledge base are the system pressure, the flow rate of the lye, the temperature of the electrolyzer, the liquid level difference between the oxygen separator and the hydrogen separator, and the oxygen in the oxygen scrubber. Medium hydrogen content, oxygen content in hydrogen in the hydrogen scrubber. Under the constraints of boundary conditions, the expected output parameters of the electrolyzer system are obtained according to the method of combining knowledge base reasoning and mathematical model, which are the given value of system pressure, the given value of lye temperature, and the given value of lye flow.
各步骤如下:The steps are as follows:
①建立电解水制氢系统基本知识库①Establish the basic knowledge base of electrolyzed water hydrogen production system
通过大量的实验,在电解槽输入不同范围功率(20%,40%,60%, 80%,100%)的情况下,通过改变系统的压力、碱液温度、碱液流量参数,电解槽系统在边界条件的限制下可以稳定运行,其中边界条件就是氧气洗涤器中的氧中氢含量要小于2%(50%LFL),氢气洗涤器中的氢中氧含量要小于0.5%,另外氧分离器液位和氢分离器的液位差要在5cm之内,碱液流量在3-4.5m3/h以内,碱液温度要保持在65℃左右,上下波动范围保持在1.1℃,电解槽温度要小于85℃等。图2-图 6分别为通过实验得到的,下面依次介绍其代表含义。Through a large number of experiments, under the condition that the electrolyzer input power in different ranges (20%, 40%, 60%, 80%, 100%), by changing the system pressure, lye temperature, lye flow parameters, the electrolyzer system It can operate stably under the limitation of boundary conditions. The boundary conditions are that the hydrogen content in oxygen in the oxygen scrubber is less than 2% (50% LFL), the oxygen content in hydrogen in the hydrogen scrubber is less than 0.5%, and the oxygen separation The liquid level difference between the liquid level of the device and the hydrogen separator should be within 5cm, the flow rate of the lye should be within 3-4.5m 3 /h, the temperature of the lye should be kept at about 65°C, and the fluctuation range should be kept at 1.1°C. The temperature should be less than 85 ℃ and so on. Figures 2 to 6 are obtained through experiments, respectively, and their representative meanings are introduced in turn below.
图2为电解槽输入不同范围功率和通过改变系统不同压力下的氧中氢含量变化图,可以看出,在电解槽输入不同范围功率的情况下,在当前系统压力(氧气分离器中的压力)下,如果氧中氢含量超出安全范围2%(50%LFL)通过适当改变系统压力,可以让氧中氢含量回到安全范围内。Figure 2 shows the change of hydrogen content in oxygen in different ranges of power input to the electrolyzer and by changing the system under different pressures. ), if the hydrogen content in oxygen exceeds the safe range by 2% (50% LFL), by appropriately changing the system pressure, the hydrogen content in oxygen can be brought back to the safe range.
在每个功率测试下,电解槽均连续运行超过两小时,以保证在此功率下电解槽可以长期运行。例如在电解槽输入功率为额定功率40%的情况下,如果系统压力为1.6Mpa,此时氧气洗涤器中的氧中氢含量已经超出2%,通过改变系统的压力为1.0Mpa,可以在图2中看出氧中氢浓度降到2%以下,系统回到安全范围内,因此当氧中氢浓度不在安全范围内时,通过适当改变系统中的压力可以保证系统的安全稳定运行,并基于此建立电解槽不同输入功率和不同系统压力下氧中氢浓度的安全区域。At each power test, the electrolyzer was run continuously for more than two hours to ensure long-term operation of the electrolyzer at this power. For example, when the input power of the electrolyzer is 40% of the rated power, if the system pressure is 1.6Mpa, the hydrogen content in the oxygen in the oxygen scrubber has exceeded 2%. By changing the system pressure to 1.0Mpa, it can be shown in Fig. It can be seen in 2 that the hydrogen concentration in oxygen drops below 2%, and the system returns to the safe range. Therefore, when the hydrogen concentration in oxygen is not within the safe range, the safe and stable operation of the system can be ensured by appropriately changing the pressure in the system. This establishes a safe area for the concentration of hydrogen in oxygen at different input powers of the electrolyzer and at different system pressures.
如图3所示,当LFL取50%时红色区域为氧中氢含量在安全范围内的区域;LFL取75%时红色和蓝色为氧中氢含量在安全范围内的区域;3区域为无法检测到的区域;4区域为不安全的区域;5区域为暂时可用的区域。As shown in Figure 3, when the LFL is 50%, the red area is the area where the hydrogen content in oxygen is within the safe range; when the LFL is 75%, the red and blue areas are the area where the hydrogen content in oxygen is within the safe range; the 3 area is Undetectable area; 4 area is unsafe area; 5 area is temporarily available area.
图4为电解槽输入不同范围功率和改变系统不同压力情况下的氢气洗涤器中的氢中氧含量变化,从图4中可以发现,氢中氧的浓度可以很好的保持在安全范围之内,在电解槽输入功率确定时,通过改变系统的压力可以降低氢气洗涤器中的氢中氧含量。为了提高电解水制氢系统产生氢气的浓度,当电解槽系统中的氢中氧含量超出氢气纯度要求(<0.5%)时,可以通过调节系统的压力来达到调节氢中氧含量的目的,从而提高系统制氢的纯度。Figure 4 shows the change of oxygen content in hydrogen in the hydrogen scrubber when the electrolyzer inputs different ranges of power and changes the system pressure. It can be found from Figure 4 that the concentration of oxygen in hydrogen can be well maintained within a safe range , when the input power of the electrolyzer is determined, the oxygen content in the hydrogen in the hydrogen scrubber can be reduced by changing the pressure of the system. In order to improve the concentration of hydrogen produced by the water electrolysis hydrogen production system, when the oxygen content in the hydrogen in the electrolysis cell system exceeds the hydrogen purity requirement (<0.5%), the purpose of adjusting the oxygen content in the hydrogen can be achieved by adjusting the pressure of the system, thereby Improve the purity of hydrogen produced by the system.
图5为电解槽输入不同范围功率和不同压力下的氧气分离器和氢气分离器液位差之间的变化,要求电解水制氢系统的氢氧分离器的液位差接近于零,偏差不超过0.7cm,图5中所示最大的液位偏差也没超过0.7cm,符合要求,因此得出电解槽的输入功率和系统压力对氢氧分离器的液位差没有明显的相关性,从而可以通过在不同功率下调节系统的压力而满足氧中氢含量的安全范围。图6展示了在不同的功率和系统压力下系统消耗的功率与能效,随着功率的升高,电堆能耗呈上升趋势而能效呈下降趋势;而系统压力的改变对这两个指标都没有明显的影响,因此也说明了可以通过调节系统压力而满足氧中氢含量的安全范围。Figure 5 shows the change between the liquid level difference between the oxygen separator and the hydrogen separator under different power ranges and different pressures input to the electrolyzer. If it exceeds 0.7cm, the maximum liquid level deviation shown in Figure 5 does not exceed 0.7cm, which meets the requirements. Therefore, it is concluded that the input power of the electrolyzer and the system pressure have no obvious correlation with the liquid level difference of the hydrogen-oxygen separator, so The safe range of hydrogen content in oxygen can be met by adjusting the pressure of the system at different powers. Figure 6 shows the power consumption and energy efficiency of the system under different power and system pressure. With the increase of power, the energy consumption of the stack shows an upward trend and the energy efficiency shows a downward trend; and the change of system pressure has a significant impact on both indicators. There is no apparent effect, thus also illustrating that the safe range of hydrogen in oxygen can be met by adjusting the system pressure.
表1-表2为不同碱液流量下的电解槽中的氧槽温和氢槽温的变化以及分离器中氢气纯度和氧气纯度的变化,从表1中可以看出碱液流量越大,氧槽温和氢槽温就越低,而碱液流量在2.6m3/h时,槽温已经超过了85℃,不在电解槽工作温度安全范围内,不利于电解槽系统的安全运行;表2中,随着碱液流量增加,氧气分离器和氢气分离器中的氧气纯度和氢气纯度略微下降,所以可以通过控制碱液流量可以达到调节电解槽温度和氧气和氢气纯度的作用。因此也可以通过在不同的工作功率下调节碱液流量从而改变氧中氢的含量,也可以控制其在2%(50%LFL)。这样一来就可以不单单通过改变系统压力来控制氧中氢的含量,将系统压力和碱液流量两者结合起来控制可以拓宽功率的调节范围。Table 1-Table 2 shows the changes of oxygen tank temperature and hydrogen tank temperature in the electrolyzer under different lye flow rates and the changes of hydrogen purity and oxygen purity in the separator. It can be seen from Table 1 that the larger the lye flow rate, the more oxygen The lower the bath temperature and the hydrogen bath temperature, and when the lye flow rate is 2.6m 3 /h, the bath temperature has exceeded 85℃, which is not within the safe range of the working temperature of the electrolyzer, which is not conducive to the safe operation of the electrolyzer system; in Table 2 , with the increase of lye flow, the oxygen purity and hydrogen purity in the oxygen separator and hydrogen separator decrease slightly, so the temperature of the electrolyzer and the purity of oxygen and hydrogen can be adjusted by controlling the lye flow. Therefore, the hydrogen content in the oxygen can also be changed by adjusting the lye flow rate under different working power, and it can also be controlled at 2% (50% LFL). In this way, it is not only possible to control the hydrogen content in oxygen by changing the system pressure, but to combine the system pressure and the lye flow to control the power adjustment range.
表1Table 1
表2Table 2
基于此,根据大量实验所得到的经验建立原始的专家经验知识库,专家经验知识库可以表示如下:Based on this, an original expert experience knowledge base is established according to the experience obtained from a large number of experiments. The expert experience knowledge base can be expressed as follows:
Ek={Tk,Pk,Yk,Bk,Zk,Sk}E k ={T k ,P k ,Y k ,B k ,Z k ,S k }
式中,Ek为第K个专家经验知识(K=1,2,3,...,m,m为专家经验知识数量);Tk为专家经验知识Ek的存储时间,Pk为专家经验知识 Ek的输入功率占额定功率的比值,Yk={yk1,yk2,yk3,yk4,yk5,yk6}为专家经验知识Ek的电解槽系统运行时的特征参数,yk1,yk2,…,yk6分别表示第 K个专家经验知识中电解槽系统安全稳定运行下的系统压力、碱液流量、电解槽温度、氧分离器和氢分离器液位差、氧中氢含量、氢中氧含量。Bk={bk1,bk2,bk3,bk4,bk5}为专家经验知识Ek中电解槽系统稳定运行时的重要参数的边界条件,bk1,bk2,,bk5分别表示氧气洗涤器中的氧中氢含量<2%、氢气洗涤器中的氢中氧含量<0.5%、3m3/h≤碱液流量≤4.5m3/h、氧分离器和氢分离器的液位差<5cm,63.9℃≤碱液温度≤66.1℃。Zk={zk1,zk2,zk3}为专家经验知识输出的期望值,zk1,zk2,zk3分别表示为系统压力给定值、碱液温度给定值、碱液流量给定值。Sk为电解槽系统当前各个特征参数情况与第K个专家经验知识的综合相似度。一个专家经验知识Ek的输入和输出如表3所示。In the formula, E k is the Kth expert experience knowledge (K=1, 2, 3, ..., m, m is the quantity of expert experience knowledge); T k is the storage time of expert experience knowledge E k , and P k is The ratio of the input power of the expert experience knowledge E k to the rated power, Y k = {y k1 , y k2 , y k3 , y k4 , y k5 , y k6 } is the characteristic of the electrolytic cell system of the expert experience knowledge E k during operation The parameters, y k1 , y k2 ,…, y k6 respectively represent the system pressure, lye flow rate, electrolyzer temperature, oxygen separator and hydrogen separator liquid level difference under the safe and stable operation of the electrolyzer system in the Kth expert’s experience and knowledge , hydrogen content in oxygen, oxygen content in hydrogen. B k ={b k1 ,b k2 ,b k3 ,b k4 ,b k5 } is the boundary condition of the important parameters of the electrolytic cell system in the expert experience knowledge E k when the electrolytic cell system runs stably, b k1 , b k2 , and b k5 respectively represent The hydrogen content in the oxygen in the oxygen scrubber is less than 2%, the oxygen content in the hydrogen in the hydrogen scrubber is less than 0.5%, 3m 3 /h ≤ lye flow rate ≤ 4.5m 3 /h, the liquid in the oxygen separator and the hydrogen separator Potential difference <5cm, 63.9℃≤lye temperature≤66.1℃. Z k = {z k1 , z k2 , z k3 } is the expected value of expert experience and knowledge output, z k1 , z k2 , z k3 are respectively expressed as a given value of system pressure, a given value of lye temperature, and a given lye flow rate value. Sk is the comprehensive similarity between the current characteristic parameters of the electrolytic cell system and the Kth expert's experience and knowledge. The input and output of an expert's experience knowledge E k are shown in Table 3.
表3table 3
查询与匹配单元:Query and match unit:
本实施例采用多属性相似度计算通过当前电解槽系统运行特征参数在符合安全边界条件里的知识库中对专家经验知识进行查询和匹配,筛选出知识库中与当前电解槽工况最为相近的期望输出值(如图8)。首先设定当前电解槽系统所处情况定义为专家经验知识En, Pn即为当前情况下的电解槽功率输入占比,Yn={yn1,yn2,…,yn6}为当前情况电解槽系统的各个参数值,首先,对于电解槽输入功率属性根据优化后的最相邻算法来计算输入功率和所有专家经验知识的相似度,从而确定出当前电解槽输入功率所处的相邻功率范围内的专家经验知识。优化后的最相邻算法如下:In this embodiment, the multi-attribute similarity calculation is used to query and match the expert experience knowledge in the knowledge base that meets the safety boundary conditions through the operating characteristic parameters of the current electrolytic cell system, and screen out the knowledge base that is most similar to the current electrolytic cell operating conditions. Expected output value (Figure 8). First, the current situation of the electrolytic cell system is defined as expert experience knowledge En , P n is the power input ratio of the electrolytic cell under the current situation, and Y n ={y n1 ,y n2 ,...,y n6 } is the current For each parameter value of the electrolytic cell system, first, for the input power attribute of the electrolytic cell, the similarity between the input power and all expert experience knowledge is calculated according to the optimized nearest neighbor algorithm, so as to determine the phase of the current electrolytic cell input power. Expert experience and knowledge in the adjacent power range. The optimized nearest neighbor algorithm is as follows:
指数形式可以使相似度计算更加准确,sim(Pi,k,Pi,n)表示专家经验知识Ek的输入功率与当前情况输入功率的相似度。找出当前情况下输入功率相邻范围的专家经验知识。其中电解槽系统的各项特征参数可能会缺失或者特征属性值为0,从而特征信息不完全,影响相似度计算,因此加入结构相似度来降低这种影响。The exponential form can make the similarity calculation more accurate, sim(P i,k ,P i,n ) represents the similarity between the input power of the expert experience knowledge E k and the input power of the current situation. Find out expert knowledge of the adjacent range of input power in the current situation. Among them, the characteristic parameters of the electrolytic cell system may be missing or the characteristic attribute value is 0, so the characteristic information is incomplete, which affects the similarity calculation. Therefore, the structural similarity is added to reduce this effect.
结构相似度只计算当前情况与历史专家经验知识中属性值不为0 的属性相似度,可以有效避免信息不完全的问题,假设P={当前情况下电解槽系统所有非空属性集合},Q={历史专家经验知识Q中所有非空属性集合},P和Q的结构相似度S表示如下:Structural similarity only calculates the similarity between the current situation and the attributes whose attribute value is not 0 in the experience knowledge of historical experts, which can effectively avoid the problem of incomplete information. Suppose P={the set of all non-empty attributes of the electrolyzer system in the current situation}, Q ={all non-empty attribute sets in the empirical knowledge Q of historical experts}, the structural similarity S of P and Q is expressed as follows:
其中,ω∩为集合P和Q的交集中所有属性的权重值之和,ω∪为集合P和Q的并集中所有属性的权重值之和。Among them, ω ∩ is the sum of the weight values of all attributes in the intersection of sets P and Q, and ω ∪ is the sum of the weight values of all attributes in the union of sets P and Q.
电解槽系统当前参数情况和以往专家经验知识的欧氏距离公式为:The Euclidean distance formula for the current parameters of the electrolytic cell system and the previous expert experience knowledge is:
其中ωi表示专家经验知识的特征权重值,通过专家实验经验可以得出系统压力特征对对电解槽系统的重要参数影响很大,在给定电解槽功率确定的情况下,在当前的系统压力情况下,电解槽系统中的氧中氢含量不在安全范围内,通过适度调整系统压力就可以使氧中氢含量在安全范围内,如图2所示。而碱液流量和系统液位相比于系统压力对重要参数的影响不大,基于此,根据对电解系统安全运行的影响程度将ωi设定为:ωi={0.9,0.05,0.05,0,0,0}。Among them, ω i represents the feature weight value of expert experience knowledge. Through expert experimental experience, it can be concluded that the system pressure characteristics have a great influence on the important parameters of the electrolytic cell system. When the power of the given electrolytic cell is determined, the current system pressure Under certain circumstances, the hydrogen content in the oxygen in the electrolyzer system is not within the safe range, and the hydrogen content in the oxygen can be kept within the safe range by moderately adjusting the system pressure, as shown in Figure 2. Compared with the system pressure, the lye flow and system liquid level have little influence on important parameters. Based on this, according to the degree of influence on the safe operation of the electrolysis system, ω i is set as: ω i ={0.9, 0.05, 0.05, 0, 0, 0}.
将最邻近算法、欧氏距离和结构相似度相结合得到电解槽当前情况与历史专家经验知识的整体相似度:Combining the nearest neighbor algorithm, Euclidean distance and structural similarity to obtain the overall similarity between the current situation of the electrolyzer and the experience knowledge of historical experts:
假设simmax为当前电解槽系统情况与历史专家经验知识相似度的最大值,即:Suppose sim max is the maximum similarity between the current electrolyzer system situation and historical expert experience knowledge, namely:
综合相似度阈值simyz可以设置为:The comprehensive similarity threshold sim yz can be set as:
其中阈值YYZ由专家经验给定,这里设置为0.9。从专家经验知识库中检索出所有整体相似度sim(En,Ek≥simyz)的专家经验知识,然后记录专家经验知识的解{Zk},时间Tk以及整体相似度sim(En,Ek),然后按照“整体相似度”、“专家经验知识存储时间”属性值降序排列,等待下一步的处理。The threshold Y YZ is given by expert experience, and is set to 0.9 here. Retrieve all the expert experience knowledge of the overall similarity sim (E n , E k ≥sim yz ) from the expert experience knowledge base, and then record the solution {Z k } of the expert experience knowledge, time T k and the overall similarity sim (E n , E k ), and then arrange them in descending order according to the attribute values of “overall similarity” and “expert experience and knowledge storage time”, and wait for the next processing.
专家经验知识重用:Expert experience and knowledge reuse:
从匹配的专家经验知识中选择出具有最大相似度simmax的专家经验知识并确定其个数Num。From the matched expert experience knowledge, select the expert experience knowledge with the maximum similarity sim max and determine its number Num.
如果Num=1,表示具有最大相似度的专家经验知识只有一个,设这个专家经验知识为Ek,1≤k≤m,令匹配专家经验知识数据表中专家经验知识Ek的下一个专家经验知识为Eh,1≤h≤m,因为匹配专家经验知识检索出来时按照“整体相似度”、“专家经验知识存储时间”的属性值进行降序排列,故Eh应该为第二大相似度并且为专家经验知识存储时间最新的一个。记专家经验知识Eh的期望输出为Zh、整体相似度为simh,专家经验知识Ek的期望输出为Zk,那么当前情况下的描述的期望输出Zhk为:If Num=1, it means that there is only one expert experience knowledge with the greatest similarity. Let this expert experience knowledge be E k , 1≤k≤m, let the next expert experience matching the expert experience knowledge E k in the expert experience knowledge data table The knowledge is E h , 1≤h≤m, because the matching expert experience knowledge is retrieved in descending order according to the attribute values of "overall similarity" and "expert experience knowledge storage time", so E h should be the second largest similarity And store the latest one for expert experience knowledge. Note that the expected output of expert experience knowledge E h is Z h , the overall similarity is sim h , and the expected output of expert experience knowledge E k is Z k , then the expected output Z hk of the description in the current situation is:
如果Num>1,则说明具有相同最大整体相似度的专家经验知识有多个,设有f个,假设这些专家经验知识Ei,i=1…f按专家经验知识存储时间属性值降序排列为:E1,E2…Ef,Z1,Z2…Zf为其相应的期望输出,那么当前情况下的描述的期望输出为:If Num>1, it means that there are multiple expert experience knowledges with the same maximum overall similarity, and there are f, assuming that these expert experience knowledge E i , i=1...f is arranged in descending order of the storage time attribute value of expert experience knowledge as : E 1 , E 2 …E f , Z 1 , Z 2 … Z f are their corresponding expected outputs, then the expected output of the description in the current situation is:
其中θi为本次专家经验知识重用的时间加权系数,满足θ1≥θ2≥…≥θl,可根据具体情况或经验确定。Among them, θ i is the time weighting coefficient for the reuse of expert experience and knowledge, which satisfies θ 1 ≥ θ 2 ≥...≥ θ l , which can be determined according to specific circumstances or experience.
评价与修正单元:Evaluation and Correction Unit:
为了验证专家经验知识重用结果的有效性,必须进行专家经验知识评价与修正。第一步是对重用结果进行评价,如果成功则不必修正,否则进行专家经验知识修正,来改善设定模块的精度。本实施例中专家经验知识评价依据它在实际环境中运行效果的反馈,专家经验知识修正在执行过程出现了问题的基础上进行。In order to verify the validity of the reuse results of expert experience and knowledge, it is necessary to evaluate and correct expert experience and knowledge. The first step is to evaluate the reuse results. If it is successful, it is not necessary to modify it. Otherwise, it is necessary to modify the expert experience and knowledge to improve the accuracy of the set module. In this embodiment, the evaluation of the expert's experience and knowledge is based on the feedback of its operation effect in the actual environment, and the correction of the expert's experience and knowledge is carried out on the basis of problems in the execution process.
电解槽系统运行后,氧中氢含量,氢中氧含量,液位差以及碱液温度会有一定的滞后性,因此每隔一个小时对这四个重要参数进行检测,将四个重要参数值反馈给专家经验知识库,来判断当前情况运行状态下的重要参数是否满足边界条件,根据是否满足边界条件来判断是否对专家经验知识进行修正,若当前重要参数超出边界条件则需要对专家经验知识进行修正,例如电解槽系统运行后的氧气洗涤器中的氧中氢含量超过2%的限制,则会影响系统运行,并且会对专家经验知识进行修正,如果重要参数都在边界条件内,则不需要对专家经验知识进行修正。After the electrolyzer system is running, the hydrogen content in oxygen, the oxygen content in hydrogen, the liquid level difference and the temperature of the lye will have a certain hysteresis. Therefore, these four important parameters are detected every one hour, and the values Feedback to the expert experience knowledge base to judge whether the important parameters in the current operating state meet the boundary conditions, and judge whether to modify the expert experience knowledge according to whether the boundary conditions are met. If the current important parameters exceed the boundary conditions, the expert experience knowledge is required. Make corrections, such as the hydrogen content in oxygen in the oxygen scrubber after the electrolyzer system is operating exceeds the limit of 2%, it will affect the system operation, and the expert experience knowledge will be corrected, if the important parameters are all within the boundary conditions, then No revision of expert experience knowledge is required.
存储与添加单元:Store and add units:
对于新专家经验知识加入历史专家经验知识库的情况,首先计算新专家经验知识和历史专家经验知识库中存储的所有专家经验知识的整体相似度,如果求出的所有相似度都小于或等于某一个给定的阈值(取阈值为0.8),则加入新专家经验知识,若至少存在一个相似度大于该阈值,则不进行存储。For the case where the new expert experience knowledge is added to the historical expert experience knowledge base, first calculate the overall similarity between the new expert experience knowledge and all the expert experience knowledge stored in the historical expert experience knowledge base, if all the obtained similarities are less than or equal to a certain A given threshold (the threshold is 0.8), new expert experience knowledge is added, and if there is at least one similarity greater than the threshold, it will not be stored.
(2)回馈补偿模型(2) Feedback compensation model
在将专家经验知识库中筛选出来的期望输出参数给到电解槽后,电解槽在运行期间,一些参数的变化可能会对系统的安全问题造成严重影响。其中对系统安全最有影响的四个重要参数为氧气洗涤器中的氧中氢含量、氢气洗涤器中的氢中氧含量、氧分离器和氢分离器的液位差以及碱液温度。氧中氢含量严格要求在2%以下,氢中氧含量要在 0.5%以下,而氧分离器和氢分离器的液位差不能超过5cm,碱液温度要保持在65℃左右。After the expected output parameters selected from the expert experience knowledge base are given to the electrolyzer, during the operation of the electrolyzer, changes in some parameters may seriously affect the safety of the system. Among them, the four important parameters that have the most impact on system safety are the hydrogen content in oxygen in the oxygen scrubber, the oxygen content in hydrogen in the hydrogen scrubber, the liquid level difference between the oxygen separator and the hydrogen separator, and the temperature of the lye. The hydrogen content in oxygen is strictly required to be below 2%, the oxygen content in hydrogen must be below 0.5%, and the liquid level difference between the oxygen separator and the hydrogen separator cannot exceed 5cm, and the temperature of the lye should be maintained at about 65°C.
本实施例中为了应对重要参数超出边界条件的情况,在智能控制模型中加入了回馈补偿模型,电解槽运行后,每隔一个小时对四个重要参数进行检测,回馈补偿模型是根据电解槽运行后检测的四个重要参数与边界条件之间的偏差,通过设定的专家规则对智能控制系统各参数给定值进行修正,使得影响系统安全和制氢纯度的参数返回安全范围内。In this embodiment, in order to deal with the situation that the important parameters exceed the boundary conditions, a feedback compensation model is added to the intelligent control model. After the electrolytic cell is running, four important parameters are detected every one hour. The feedback compensation model is based on the operation of the electrolytic cell. The deviation between the four important parameters detected later and the boundary conditions is corrected by the set expert rules to the given values of the parameters of the intelligent control system, so that the parameters affecting the safety of the system and the purity of hydrogen production are returned to the safe range.
回馈补偿模型主要分为三部分,分别是:The feedback compensation model is mainly divided into three parts:
专家规则建立单元:Expert rule building unit:
专家通过实际经验和大量实验对电解槽运行后输出的四个重要参数与边界值之间的偏差(△e1、△e2、△e3、△e4)设置规则,规则表如表4所示。其中△e1、△e2、△e3、△e4分别是电解槽运行中的氧中氢含量与边界值2%之间的误差、电解槽运行中的氢中氧含量与边界值0.5%之间的误差、电解槽运行中的液位差与边界值5cm之间的误差,电解槽运行中的碱液温度和边界值65℃之间的误差△p、△f、△T分别表示依据专家经验得到的系统压力补偿值、碱液流量补偿值、碱液温度补偿值k1,1,k1,2,...,k4,1,k4,2分别表示针对四种不同偏差,专家根据经验和规律,对每种偏差给出三个电解槽给定参数补偿的相关系数。Experts set rules for the deviations (△e1, △e2, △e3, △e4) between the four important parameters output after the electrolyzer runs and the boundary values through practical experience and a large number of experiments. The rule table is shown in Table 4. Among them, △e1, △e2, △e3, and △e4 are the error between the hydrogen content of the oxygen in the electrolyzer operation and the boundary value of 2%, and the difference between the oxygen content of the hydrogen in the electrolyzer operation and the boundary value of 0.5%, respectively. Error, the error between the liquid level difference in the operation of the electrolyzer and the boundary value of 5cm, the error between the temperature of the lye solution in the operation of the electrolyzer and the boundary value of 65℃ The system pressure compensation value, lye liquid flow compensation value, and lye liquid temperature compensation value k 1,1 ,k 1,2 ,...,k 4,1 ,k 4,2 respectively represent four different deviations, experts according to Based on experience and rules, the correlation coefficients for the compensation of the given parameters of the three electrolyzers are given for each type of deviation.
表4Table 4
推理机单元:Inference engine unit:
推理机根据电解槽运行中输出的四个重要参数与边界值之间的差值,通过专家经验规则采用穷尽式逐项搜索算法推理出相应的专家经验补偿值。将推理机推理出的专家经验补偿值输出。The reasoning engine infers the corresponding expert experience compensation value by using the exhaustive item-by-item search algorithm through expert experience rules according to the difference between the four important parameters output during the operation of the electrolyzer and the boundary value. Output the expert experience compensation value deduced by the inference engine.
电解水制氢模块:Electrolyzed water hydrogen production module:
电解水制氢模块根据专家经验知识库模型系统和回馈补偿模型修正的电解槽系统各项给定参数,包括系统压力给定值、碱液温度给定值、碱液流量给定值,通过模糊规则和神经网络结合来对电解槽系统中的压力调节阀以及气动调节阀等进行瞬态PID控制,来保证电解槽系统此时的压力、氧分离器和氢分离器的液位以及碱液温度和流量都可以快速的响应去趋于各项参数的给定值,保证了电解槽制氢系统在输入功率波动下的安全稳定运行。同时电解槽运行后,因为参数变化会有滞后性,故每隔一个小时对四个参数进行检测,并将检测的四个参数值输出到专家经验知识库模型中,这四个参数分别是氧气洗涤器中氧中氢含量,氢气洗涤器中氢中氧含量,氧分离器和氢分离器之间的液位差以及碱液温度。将这四个参数输出到专家经验知识库模型的原因是:判断是否在边界范围内,如果在范围内,则系统正常运行,专家经验知识不需要修正。如果不在边界范围内,则需要对专家经验知识进行修正。The given parameters of the electrolyzer system, including the given value of system pressure, the given value of lye temperature, and the given value of lye flow, are corrected by the electrolysis water hydrogen production module according to the expert experience knowledge base model system and the feedback compensation model. The rules and neural network are combined to perform transient PID control on the pressure regulating valve and pneumatic regulating valve in the electrolyzer system to ensure the pressure of the electrolyzer system, the liquid level of the oxygen separator and the hydrogen separator and the temperature of the lye at this time. And the flow rate can respond quickly to tend to the given value of each parameter, which ensures the safe and stable operation of the electrolyzer hydrogen production system under the fluctuation of input power. At the same time, after the electrolyzer is running, because the parameter changes will have hysteresis, the four parameters are detected every one hour, and the detected four parameters are output to the expert experience knowledge base model. The four parameters are oxygen The hydrogen content in the oxygen in the scrubber, the oxygen content in the hydrogen in the hydrogen scrubber, the liquid level difference between the oxygen separator and the hydrogen separator, and the lye temperature. The reason for outputting these four parameters to the expert experience knowledge base model is to judge whether it is within the boundary range. If it is not within the bounds, the expert experience knowledge needs to be corrected.
如图7,本实施例还提供适应宽功率波动的电解水制氢智能自适应控制方法,包括:As shown in Figure 7, this embodiment also provides an intelligent adaptive control method for electrolyzed water for hydrogen production that adapts to wide power fluctuations, including:
电解水制氢系统根据专家经验知识库模型系统和回馈补偿模型修正的电解槽系统各项给定参数,通过模糊规则和神经网络结合来对电解槽系统中的压力调节阀以及气动调节阀等进行瞬态PID控制,同时每隔一个小时输出四个边界重要参数检测值到回馈补偿模型和专家经验知识库模型中。其中输出到回馈补偿模型的目的是根据四个重要参数与边界条件之间的偏差根据设置的专家经验规则得出四个重要参数的补偿值;输出到专家经验知识库模型的目的是判断当前参数检测值是否在边界范围内,如果在范围内,则系统正常运行,专家经验知识不需要修正。如果不在边界范围内,则需要对专家经验知识进行修正。The electrolytic water hydrogen production system is based on the expert experience knowledge base model system and the feedback compensation model to correct the given parameters of the electrolytic cell system, and the pressure regulating valve and pneumatic regulating valve in the electrolytic cell system are combined with fuzzy rules and neural networks. Transient PID control, and output four boundary important parameter detection values to the feedback compensation model and the expert experience knowledge base model every hour. The purpose of outputting to the feedback compensation model is to obtain the compensation values of the four important parameters according to the deviation between the four important parameters and the boundary conditions according to the set expert experience rules; the purpose of outputting to the expert experience knowledge base model is to judge the current parameters Check whether the detected value is within the boundary range. If it is within the range, the system is running normally, and expert experience and knowledge do not need to be corrected. If it is not within the bounds, the expert experience knowledge needs to be corrected.
本发明提出的适应宽功率波动的电解水制氢智能自适应控制方法可以在适应可再生能源发电不确定性导致碱性电解槽宽功率波动的基础上,通过智能控制方法自适应的控制电解槽给定参数(系统压力、碱液流量、碱液温度)使电解槽系统的重要参数(氧中氢含量等) 保持在安全范围内,达到电解槽系统在保证安全稳定运行的条件下,有效的提高了电解槽的制氢效率和制出氢气纯度。The intelligent self-adaptive control method for hydrogen production by electrolysis of water adapted to wide power fluctuations proposed by the invention can adaptively control the electrolyzer through the intelligent control method on the basis of adapting to the wide power fluctuation of the alkaline electrolyzer caused by the uncertainty of renewable energy power generation Given parameters (system pressure, lye flow, lye temperature), the important parameters of the electrolyzer system (hydrogen content in oxygen, etc.) are kept within a safe range, so that the electrolyzer system can effectively operate under the condition of ensuring safe and stable operation. The hydrogen production efficiency and the produced hydrogen purity of the electrolyzer are improved.
以上所述的实施例仅是对本发明优选方式进行的描述,并非对本发明的范围进行限定,在不脱离本发明设计精神的前提下,本领域普通技术人员对本发明的技术方案做出的各种变形和改进,均应落入本发明权利要求书确定的保护范围内。The above-mentioned embodiments are only descriptions of the preferred modes of the present invention, and do not limit the scope of the present invention. Without departing from the design spirit of the present invention, those of ordinary skill in the art can make various Variations and improvements should fall within the protection scope determined by the claims of the present invention.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN117472122A (en) * | 2023-10-08 | 2024-01-30 | 三峡科技有限责任公司 | MW alkaline water electrolysis system operation control optimization method |
EP4382639A3 (en) * | 2022-12-06 | 2024-09-11 | Solaredge Technologies Ltd. | Control of variable power source-coupled electrolysers |
Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2017149606A1 (en) * | 2016-02-29 | 2019-01-17 | 株式会社東芝 | Hydrogen production system and hydrogen production method |
CN111826669A (en) * | 2020-03-31 | 2020-10-27 | 同济大学 | Large-scale electrolyzed water hydrogen production system and control method with wide power fluctuation adaptability |
CN112481637A (en) * | 2020-11-10 | 2021-03-12 | 安徽伯华氢能源科技有限公司 | Water electrolysis hydrogen production system for fluctuating power supply and control strategy thereof |
CN113162022A (en) * | 2021-02-26 | 2021-07-23 | 河北建投新能源有限公司 | Power configuration method and device for photovoltaic hydrogen generation station |
CN113325712A (en) * | 2021-05-28 | 2021-08-31 | 全球能源互联网研究院有限公司 | Self-adaptive response control method, system and device in electrolytic hydrogen production system |
CN113373457A (en) * | 2021-06-11 | 2021-09-10 | 河北建投新能源有限公司 | Control method and device for hydrogen production by water electrolysis and computer readable storage medium |
CN113403645A (en) * | 2021-06-23 | 2021-09-17 | 阳光电源股份有限公司 | Method and device for determining working state of electrolytic cell and controller |
CN113549953A (en) * | 2021-08-16 | 2021-10-26 | 阳光电源股份有限公司 | Liquid level balance control method of hydrogen production system and hydrogen production system |
CN113930784A (en) * | 2021-10-15 | 2022-01-14 | 国网浙江省电力有限公司嘉善县供电公司 | Hydrogen production system for PEM (proton exchange membrane) water electrolysis and regulation and optimization method |
CN114075677A (en) * | 2021-10-14 | 2022-02-22 | 清华大学 | Parameter control method, device, equipment and storage medium for hydrogen production system |
CN114086204A (en) * | 2021-12-10 | 2022-02-25 | 清华四川能源互联网研究院 | A kind of electrolyzer array system and electrolyzed water system control method |
CN114525520A (en) * | 2022-03-07 | 2022-05-24 | 阳光氢能科技有限公司 | Hydrogen production system heat standby control method and hydrogen production system |
CN114592207A (en) * | 2022-04-06 | 2022-06-07 | 中国船舶重工集团公司第七一八研究所 | Electrolytic hydrogen production system adapting to rapid wide power fluctuation and control method |
-
2022
- 2022-06-23 CN CN202210716791.2A patent/CN115074776B/en active Active
Patent Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPWO2017149606A1 (en) * | 2016-02-29 | 2019-01-17 | 株式会社東芝 | Hydrogen production system and hydrogen production method |
CN111826669A (en) * | 2020-03-31 | 2020-10-27 | 同济大学 | Large-scale electrolyzed water hydrogen production system and control method with wide power fluctuation adaptability |
CN112481637A (en) * | 2020-11-10 | 2021-03-12 | 安徽伯华氢能源科技有限公司 | Water electrolysis hydrogen production system for fluctuating power supply and control strategy thereof |
CN113162022A (en) * | 2021-02-26 | 2021-07-23 | 河北建投新能源有限公司 | Power configuration method and device for photovoltaic hydrogen generation station |
CN113325712A (en) * | 2021-05-28 | 2021-08-31 | 全球能源互联网研究院有限公司 | Self-adaptive response control method, system and device in electrolytic hydrogen production system |
CN113373457A (en) * | 2021-06-11 | 2021-09-10 | 河北建投新能源有限公司 | Control method and device for hydrogen production by water electrolysis and computer readable storage medium |
CN113403645A (en) * | 2021-06-23 | 2021-09-17 | 阳光电源股份有限公司 | Method and device for determining working state of electrolytic cell and controller |
CN113549953A (en) * | 2021-08-16 | 2021-10-26 | 阳光电源股份有限公司 | Liquid level balance control method of hydrogen production system and hydrogen production system |
CN114075677A (en) * | 2021-10-14 | 2022-02-22 | 清华大学 | Parameter control method, device, equipment and storage medium for hydrogen production system |
CN113930784A (en) * | 2021-10-15 | 2022-01-14 | 国网浙江省电力有限公司嘉善县供电公司 | Hydrogen production system for PEM (proton exchange membrane) water electrolysis and regulation and optimization method |
CN114086204A (en) * | 2021-12-10 | 2022-02-25 | 清华四川能源互联网研究院 | A kind of electrolyzer array system and electrolyzed water system control method |
CN114525520A (en) * | 2022-03-07 | 2022-05-24 | 阳光氢能科技有限公司 | Hydrogen production system heat standby control method and hydrogen production system |
CN114592207A (en) * | 2022-04-06 | 2022-06-07 | 中国船舶重工集团公司第七一八研究所 | Electrolytic hydrogen production system adapting to rapid wide power fluctuation and control method |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4382639A3 (en) * | 2022-12-06 | 2024-09-11 | Solaredge Technologies Ltd. | Control of variable power source-coupled electrolysers |
CN117472122A (en) * | 2023-10-08 | 2024-01-30 | 三峡科技有限责任公司 | MW alkaline water electrolysis system operation control optimization method |
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