Aspen Plus model of an alkaline electrolysis system for hydrogen production

被引:204
作者
Sanchez, Monica [1 ,2 ]
Amores, Ernesto [1 ]
Abad, David [1 ]
Rodriguez, Lourdes [3 ]
Clemente-Jul, Carmen [2 ]
机构
[1] Ctr Nacl Hidrogeno CNH2, Prolongacion Fernando El Santo S-N, Ciudad Real 13500, Spain
[2] UPM, Dept Energia & Combustibles, ETSI Minas & Energia, C Rios Rosas 21, Madrid 28003, Spain
[3] UEM, C Tajo S-N, Madrid 28670, Spain
关键词
Hydrogen production; Alkaline water electrolysis; Balance of plant; System simulation; Aspen plus model; Process optimization; WATER ELECTROLYSIS; ENERGY; POWER; PERFORMANCE; SIMULATION; OPERATION; STORAGE; CELL; GAS;
D O I
10.1016/j.ijhydene.2019.12.027
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
A model of an alkaline electrolysis plant is proposed in this paper, including both stack and balance of plant, with the objective of analyzing the performance of a complete electrolysis system. For this purpose, Aspen Plus has been used in this work due to its great potential and flexibility. Since this software does not include codes for modelling the electrolysis cells, a custom model for the stack has been integrated as a subroutine, using a tool called Aspen Custom Modeler. This stack model is based on semi-empirical equations which describe the voltage cell, Faraday efficiency and gas purity as a function of the current. The rest of the components in the electrolysis plant have been modelled with standard operation units included in Aspen Plus. Simulations have been carried out in order to evaluate and optimize the balance of the plant of an alkaline electrolysis system for hydrogen production. Also, a parametric study has been conducted. The results show that increasing the operation temperature and reducing the pressure can improve the overall performance of the system. The proposed model in this work for the alkaline electrolyzer can be used in the future to develop a useful tool to carry out techno-economic studies of alkaline electrolysis systems integrated with other process. (C) 2019 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:3916 / 3929
页数:14
相关论文
共 51 条
[1]   Energy and exergy utilizations of the US manufacturing sector [J].
Al-Ghandoor, A. ;
Phelan, P. E. ;
Villalobos, R. ;
Jaber, J. O. .
ENERGY, 2010, 35 (07) :3048-3065
[2]  
Amores E, 2017, OPEN ENG, V7, P141, DOI 10.1515/eng-2017-0020
[3]   Influence of operation parameters in the modeling of alkaline water electrolyzers for hydrogen production [J].
Amores, Ernesto ;
Rodriguez, Jesus ;
Carreras, Christian .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2014, 39 (25) :13063-13078
[4]   An adaptable steady state Aspen Hysys model for the methane fuelled solid oxide fuel cell [J].
Anderson, Timothy ;
Vijay, Periasamy ;
Tade, Moses O. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2014, 92 (02) :295-307
[5]   Alkaline electrolysers: Model and real data analysis [J].
Artuso, Paola ;
Gammon, Rupert ;
Orecchini, Fabio ;
Watson, Simon J. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2011, 36 (13) :7956-7962
[6]  
Bertuccioli L., 2014, DEV WATER ELECT EURO
[7]   A new approach to empirical electrical modelling of a fuel cell, an electrolyser or a regenerative fuel cell [J].
Busquet, S ;
Hubert, CE ;
Labbé, J ;
Mayer, D ;
Metkemeijer, R .
JOURNAL OF POWER SOURCES, 2004, 134 (01) :41-48
[8]   Current status of water electrolysis for energy storage, grid balancing and sector coupling via power-to-gas and power-to-liquids: A review [J].
Buttler, Alexander ;
Spliethoff, Hartmut .
RENEWABLE & SUSTAINABLE ENERGY REVIEWS, 2018, 82 :2440-2454
[9]   Thermal performance of a commercial alkaline water electrolyzer: Experimental study and mathematical modeling [J].
Dieguez, P. M. ;
Ursua, A. ;
Sanchis, P. ;
Sopena, C. ;
Guelbenzu, E. ;
Gandia, L. M. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (24) :7338-7354
[10]  
Dyment J, 2015, JUMP START ASPEN CUS