Alkaline electrolysers: Model and real data analysis

被引:31
作者
Artuso, Paola [1 ]
Gammon, Rupert [2 ]
Orecchini, Fabio [3 ]
Watson, Simon J. [4 ]
机构
[1] Sapienza Univ Rome, CIRPS, Interuniv Res Ctr Sustainable Dev, I-00184 Rome, Italy
[2] Bryte Energy Ltd, Loughborough Innovat Ctr, Loughborough LE11 3EH, Leics, England
[3] Univ Guglielmo Marconi, I-00184 Rome, Italy
[4] Univ Loughborough, Ctr Renewable Energy Syst Technol, Dept Elect & Elect Engn, Loughborough LE11 3TU, Leics, England
关键词
Alkaline electrolyser; Simulation programme; Experimental data; Electrolyser model;
D O I
10.1016/j.ijhydene.2011.01.094
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070305 [高分子化学与物理];
摘要
This paper presents an analysis of the data collected during a test of the 36 kW alkaline electrolyser at West Bacon Farm (WBF), Loughborough, UK. This data is then used to verify a software model of an electrolyser. The test consisted of collecting data under different operating conditions, in particular controlling the power supplied to the electrolyser. The experiment was divided in four phases. In the first two phases, the electrolyser was operated at full power, in the third phase it was operated at 60% of maximum power and in the forth it was operated at 20% of maximum power, which is the minimum permitted level. Each phase lasted approximately an hour. During phase 1, the initial warm up period, the voltage remained almost constant, while the current increased to a maximum of 428 A. After about an hour, the current suddenly dropped to 310 A, the voltage decreased from 92 V to 88 V and hydrogen production decreased from 7.3 Nm(3)/h to 6.6 Nm(3)/h, even though no change had been made to the control parameters, which were still set to maximum power input. The temperature continued upwards with only a slight reduction in its rate of increase and the pressure stopped rising, remaining at 22 bar(g). This point marks the transition from phase 1 to phase 2 and the reasons for the sudden discontinuity are investigated in this study. Once the optimum operating temperature was reached, during phase 2, it was maintained within a limited range by the cooling system. The initial stack temperature, at the beginning of phase 1, had been 17 degrees C. The net power draw increased until the stack temperature reached its maximum at 76 degrees C after about 1 h 20 min. Copyright (C) 2011, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:7956 / 7962
页数:7
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