Temperature and voltage dynamic control of PEMFC Stack using MPC method

被引:39
作者
Chen, Xi [1 ]
Fang, Ye [1 ]
Liu, Qinxiao [1 ]
He, Lingxuan [1 ]
Zhao, Yibo [1 ]
Huang, Taiming [1 ]
Wan, Zhongmin [1 ]
Wang, Xiaodong [2 ]
机构
[1] Hunan Inst Sci & Technol, Coll Mech Engn, Yueyang 414006, Peoples R China
[2] North China Elect Power Univ, Res Ctr Engn Thermophys, Beijing 102206, Peoples R China
基金
国家自然科学基金重大项目;
关键词
PEMFC; MPC; Voltage control; Temperature control; MODEL-PREDICTIVE CONTROL; MEMBRANE FUEL-CELL; FLOW-FIELD DESIGN; SYSTEM; OPTIMIZATION; MANAGEMENT; POWER;
D O I
10.1016/j.egyr.2021.11.271
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Proton Exchange Membrane Fuel Cell (PEMFC) is a multi-parameter and strongly coupled complex system, efficient and smooth operation is beneficial to the efficiency and stability of PEMFC. In this paper, aiming at improve the temperature and voltage management in PEMFC, a stack model is established, and a PEMFC temperature and voltage dynamic management controller based on Model Predict Control method (MPC) is proposed. The working temperature and output voltage are controlled by the mass flow rate of cooling water and hydrogen gas, respectively. The performances of PEMFC under different controller including MPC and traditional PID controllers are analyzed. Due to the optimization of future time step in MPC controller, the measured value will move close to the set value faster. The response time and overshoots of temperature and voltage are remarkably reduced. Compared with PID controller, MPC temperature control has smaller overshoot and faster response time, Moreover, with step current change, voltage overshoot of MPC controller is less than 1.2% which is better than other controllers.(c) 2021 Published by Elsevier Ltd. This is an open access article under the CC BY-NC-ND license (http://creativecommons.org/licenses/by-nc-nd/4.0/).
引用
收藏
页码:798 / 808
页数:11
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