Model Predictive Control of Hydrogen Pressure of Multi-Stack Fuel Cell System

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Abstract

To control and stabilize the hydrogen pressure in a multi-stack fuel cell system, a dynamic simulation model of a multi-stack fuel cell hydrogen system structure containing supply and exhaust common rail is built based on Matlab/Simulink. In the control method, the idea of local linearization was adopted. Local linearization models of the system around different steady-state operating points were built and model predictive controller for each interval was designed. This multi-point linearized control model can improve the solution speed and reduce the impact caused by the mismatch problem. The results show that under step operating condition, the deviation of the reactor inlet pressure can be reduced by 22.5%, and the adjustment time can be reduced from 31 to 22 seconds. Under C-WTVC operating condition, power consumption of the blower in the hydrogen system is reduced by 13.6% compared with that of the conventional PID. It is concluded that the controller designed in this paper is better than the traditional PID controller and is more suitable for the hydrogen system of the multi-stack fuel cell.
多堆燃料电池系统氢压力的模型预测控制
为了控制和稳定多堆燃料电池系统中的氢气压力,基于Matlab/Simulink建立了包含供排气共轨的多堆燃料电池氢气系统结构的动态仿真模型。在控制方法中,采用局部线性化的思想。建立了系统在不同稳态工作点附近的局部线性化模型,并设计了每个区间的模型预测控制器。这种多点线性化控制模型可以提高求解速度,减少错配问题带来的影响。结果表明,在步进工况下,反应器进口压力偏差可降低22.5%,调节时间由31秒缩短至22秒。在C-WTVC工况下,加氢系统鼓风机功耗较常规PID降低13.6%。结果表明,本文所设计的控制器优于传统的PID控制器,更适用于多堆燃料电池的氢气系统。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
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