Semiempirical model based on thermodynamic principles for determining 6 kW proton exchange membrane electrolyzer stack characteristics
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[1] J. Smith,et al. Introduction to chemical engineering thermodynamics , 1949 .
[2] C. Bowen,et al. The Thermodynamics of Aqueous Water Electrolysis , 1980 .
[3] T. Springer,et al. Polymer Electrolyte Fuel Cell Model , 1991 .
[4] A. Parthasarathy,et al. Temperature Dependence of the Electrode Kinetics of Oxygen Reduction at the Platinum/Nafion® Interface—A Microelectrode Investigation , 1992 .
[5] James Larminie,et al. Fuel Cell Systems Explained , 2000 .
[6] K. Onda,et al. Performance analysis of polymer-electrolyte water electrolysis cell at a small-unit test cell and performance prediction of large stacked cell , 2002 .
[7] D. Bessarabov,et al. A simple model for solid polymer electrolyte (SPE) water electrolysis , 2004 .
[8] D. A. Noren,et al. Clarifying the Butler–Volmer equation and related approximations for calculating activation losses in solid oxide fuel cell models , 2005 .
[9] S. Watson,et al. Comparison of electrical energy efficiency of atmospheric and high-pressure electrolysers , 2006 .
[10] H. Salehfar,et al. Semiempirical Model for Determining PEM Electrolyzer Stack Characteristics , 2006 .
[11] A. Marshall,et al. Hydrogen production by advanced proton exchange membrane (PEM) water electrolysers—Reduced energy consumption by improved electrocatalysis , 2007 .
[12] A. J. Peters,et al. A semiempirical study of the temperature dependence of the anode charge transfer coefficient of a 6 kW PEM electrolyzer , 2008 .