Design of a Pilot SOFC System for the Combined Production of Hydrogen and Electricity under Refueling Station Requirements

被引:13
作者
Perez-Fortes, M. [1 ]
Mian, A. [2 ]
Srikanth, S. [3 ]
Wang, L. [1 ,2 ]
Diethelm, S. [1 ]
Varkaraki, E. [4 ]
Mirabelli, I. [5 ]
Makkus, R. [5 ]
Schoon, R. [6 ]
Marechal, F. [2 ]
Van herle, J. [1 ]
机构
[1] Ecole Polytech Fed Lausanne, Grp Energy Mat, Rue Ind 17,Case Postale 440, CH-1951 Sion, Switzerland
[2] Ecole Polytech Fed Lausanne, Ind Proc & Energy Syst Engn, Rue Ind 17,Case Postale 440, CH-1951 Sion, Switzerland
[3] German Aerosp Ctr DLR, Inst Engn Thermodynam, Pfaffenwaldring 38-40, D-70569 Stuttgart, Germany
[4] SOLIDpower SA, Ave Sports 26, CH-1400 Yverdon Les Bain, Switzerland
[5] HyGear BV, Westervoortsedijk 73, NL-6827 AV Arnhem, Netherlands
[6] Shell Global Solut Int BV, Grasweg 31, NL-1031 HW Amsterdam, Netherlands
基金
欧盟地平线“2020”;
关键词
Conceptual Design; Electric Vehicle Station; Fuel Cell; Heat Exchanger Network (HEN); Hydrogen Refueling Station (HRS); Industrial Chemistry; Multi-Objective Optimization (MOO); Multi-Period Optimization; Process System Engineering (PSE); Solid Oxide Fuel Cell (SOFC); HEAT-EXCHANGER NETWORKS; MULTIPERIOD SEQUENTIAL SYNTHESIS; STEAM REFORMING KINETICS; OXIDE FUEL-CELLS; OPTIMAL OPERATION; UTILITY SYSTEMS; MODEL; OPTIMIZATION; SCALE;
D O I
10.1002/fuce.201800200
中图分类号
O646 [电化学、电解、磁化学];
学科分类号
081704 ;
摘要
The objective of the current work is to support the design of a pilot hydrogen and electricity producing plant that uses natural gas (or biomethane) as raw material, as a transition option towards a 100% renewable transportation system. The plant, with a solid oxide fuel cell (SOFC) as principal technology, is intended to be the main unit of an electric vehicle station. The refueling station has to work at different operation periods characterized by the hydrogen demand and the electricity needed for supply and self-consumption. The same set of heat exchangers has to satisfy the heating and cooling needs of the different operation periods. In order to optimize the operating variables of the pilot plant and to provide the best heat exchanger network, the applied methodology follows a systematic procedure for multi-objective, i.e. maximum plant efficiency and minimum number of heat exchanger matches, and multi-period optimization. The solving strategy combines process flow modeling in steady state, superstructure-based mathematical programming and the use of an evolutionary-based algorithm for optimization. The results show that the plant can reach a daily weighted efficiency exceeding 60%, up to 80% when considering heat utilization.
引用
收藏
页码:389 / 407
页数:19
相关论文
共 38 条
[1]   Simulation and Optimization of Pressure Swing Adsorption Systems Using Reduced-Order Modeling [J].
Agarwal, Anshul ;
Biegler, Lorenz T. ;
Zitney, Stephen E. .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (05) :2327-2343
[2]   Optimal operation of a photovoltaic generation-powered hydrogen production system at a hydrogen refueling station [J].
Aki, Hirohisa ;
Sugimoto, Ichiro ;
Sugai, Tokuyoshi ;
Toda, Masahisa ;
Kobayashi, Masahiro ;
Ishida, Masayoshi .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2018, 43 (32) :14892-14904
[3]  
Al Ashkar H., 2016, 2016011183 SAE, DOI [10.4271/2016-01-1183, DOI 10.4271/2016-01-1183]
[4]  
[Anonymous], 2016, MODELING LOW EMISSIO
[5]  
[Anonymous], 2012, ANAL SYNTHESIS DESIG, DOI DOI 10.5860/CHOICE.36-0974
[6]   SOFC mathematic model for systems simulations - Part 2: definition of an analytical model [J].
Bove, R ;
Lunghi, P ;
Sammes, NM .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2005, 30 (02) :189-200
[7]   Modeling solid oxide fuel cell operation: Approaches, techniques and results [J].
Bove, Roberto ;
Ubertini, Stefano .
JOURNAL OF POWER SOURCES, 2006, 159 (01) :543-559
[8]   Optimal operation of a hydrogen refuelling station combined with wind power in the electricity market [J].
Carr, Stephen ;
Zhang, Fan ;
Liu, Feng ;
Du, Zhaolong ;
Maddy, Jon .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2016, 41 (46) :21057-21066
[9]   Optimal operation of the Pressure Swing Adsorption (PSA) process for CO2 recovery [J].
Choi, WK ;
Kwon, TI ;
Yeo, YK ;
Lee, H ;
Song, HK ;
Na, BK .
KOREAN JOURNAL OF CHEMICAL ENGINEERING, 2003, 20 (04) :617-623
[10]  
Elgowainy A., 2008, P PVP2008 2008 ASME, P131