High Temperature Polymer Electrolyte Membrane Fuel Cells 2016
DOI: 10.1007/978-3-319-17082-4_18
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Approaches for the Modeling of PBI/H3PO4 Based HT-PEM Fuel Cells

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Cited by 2 publications
(3 citation statements)
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“…where K H 2 p -the permeability coefficient of hydrogen in the membrane; ν H 2 -the stoichiometry coefficient; n H 2 e -the number of electrons; P H 2 cat,j -the partial pressure of hydrogen in the anode catalyst layer. Siegel et al [25] have provided empirical correlations for calculating the permeability coefficient in an HT-MEA.…”
Section: Electrode Currentmentioning
confidence: 99%
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“…where K H 2 p -the permeability coefficient of hydrogen in the membrane; ν H 2 -the stoichiometry coefficient; n H 2 e -the number of electrons; P H 2 cat,j -the partial pressure of hydrogen in the anode catalyst layer. Siegel et al [25] have provided empirical correlations for calculating the permeability coefficient in an HT-MEA.…”
Section: Electrode Currentmentioning
confidence: 99%
“…For the potentiostatic mode, the cell voltage (E cell ) is an input parameter. In their studies, Olapade et al [25,26] presented the following empirical correlation for the ionic conductivity of the PBI membrane:…”
Section: Electrolyte Currentmentioning
confidence: 99%
“…For example, a peak power of 1.7 W cm -2 has been achieved for HT-PEMFCs using hydrogen and oxygen [5,6,7,8], while a HT-PEM ECHP has shown 1 A cm -2 at 55 mV [7]. A central advantage of HT-PEM fuel cells and hydrogen pumps is their ability to tolerate carbon monoxide (CO) in the hydrogen stream as CO adsorption at temperatures of 200 °C or above is diminished [9]. Over 90% of all hydrogen is derived from steam methane reforming (SMR) that leads to mixtures of hydrogen and CO. Electrochemical processes that can tolerate CO allow the use of low-cost hydrogen because hydrogen from SMR is about 2x to 3x cheaper than hydrogen from water electrolysis.…”
Section: Introductionmentioning
confidence: 99%