Improving the Efficiency of PEM Electrolyzers through Membrane-Specific Pressure Optimization

被引:85
作者
Scheepers, Fabian [1 ]
Staebler, Markus [1 ]
Staebler, Andrea [1 ]
Rauls, Edward [1 ]
Mueller, Martin [1 ]
Carmo, Marcelo [1 ]
Lehnert, Werner [1 ,2 ]
机构
[1] Forschungszentrum Julich, Electrochem Proc Engn, Inst Energy & Climate Res, IEK 14, D-52425 Julich, Germany
[2] Rhein Westfal TH Aachen, Fac Mech Engn, D-52072 Aachen, Germany
关键词
polymer electrolyte membrane electrolyzer; membrane; pressure operation; system optimization; system modelling; functional layer; storage pressure; WATER ELECTROLYSIS; RENEWABLE HYDROGEN; TECHNOECONOMIC ANALYSIS; ENERGY-STORAGE; CELLS; TEMPERATURE; PERMEATION; COST; PERFORMANCE; DESIGN;
D O I
10.3390/en13030612
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
Hydrogen produced in a polymer electrolyte membrane (PEM) electrolyzer must be stored under high pressure. It is discussed whether the gas should be compressed in subsequent gas compressors or by the electrolyzer. While gas compressor stages can be reduced in the case of electrochemical compression, safety problems arise for thin membranes due to the undesired permeation of hydrogen across the membrane to the oxygen side, forming an explosive gas. In this study, a PEM system is modeled to evaluate the membrane-specific total system efficiency. The optimum efficiency is given depending on the external heat requirement, permeation, cell pressure, current density, and membrane thickness. It shows that the heat requirement and hydrogen permeation dominate the maximum efficiency below 1.6 V, while, above, the cell polarization is decisive. In addition, a pressure-optimized cell operation is introduced by which the optimum cathode pressure is set as a function of current density and membrane thickness. This approach indicates that thin membranes do not provide increased safety issues compared to thick membranes. However, operating an N212-based system instead of an N117-based one can generate twice the amount of hydrogen at the same system efficiency while only one compressor stage must be added.
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页数:21
相关论文
共 56 条
[1]   Radiation-Grafted Polymer Electrolyte Membranes for Water Electrolysis Cells: Evaluation of Key Membrane Properties [J].
Albert, Albert ;
Barnett, Alejandro O. ;
Thomassen, Magnus S. ;
Schmidt, Thomas J. ;
Gubler, Lorenz .
ACS APPLIED MATERIALS & INTERFACES, 2015, 7 (40) :22203-22212
[2]  
Alduchov OA, 1996, J APPL METEOROL, V35, P601, DOI 10.1175/1520-0450(1996)035<0601:IMFAOS>2.0.CO
[3]  
2
[4]  
[Anonymous], 2003, EUR 20995EN
[5]   Dynamic modeling and simulation of a proton exchange membrane electrolyzer for hydrogen production [J].
Awasthi, A. ;
Scott, Keith ;
Basu, S. .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2011, 36 (22) :14779-14786
[6]   Perspectives on Low-Temperature Electrolysis and Potential for Renewable Hydrogen at Scale [J].
Ayers, Katherine ;
Danilovic, Nemanja ;
Ouimet, Ryan ;
Carmo, Marcelo ;
Pivovar, Bryan ;
Bornstein, Marius .
ANNUAL REVIEW OF CHEMICAL AND BIOMOLECULAR ENGINEERING, VOL 10, 2019, 10 :219-239
[7]  
Barbir F., 2013, PEM Fuel Cells, V2nd ed., P33, DOI 10.1016/C2011-0-06706-6
[8]   Energetic evaluation of high pressure PEM electrolyzer systems for intermediate storage of renewable energies [J].
Bensmann, B. ;
Hanke-Rauschenbach, R. ;
Arias, I. K. Pena ;
Sundmacher, K. .
ELECTROCHIMICA ACTA, 2013, 110 :570-580
[9]   Analysis of Voltage Losses in PEM Water Electrolyzers with Low Platinum Group Metal Loadings [J].
Bernt, Maximilian ;
Siebel, Armin ;
Gasteiger, Hubert A. .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 2018, 165 (05) :F305-F314
[10]  
Bertuccioli L, 2014, FUEL CELLS HYDROG JO, P1