1996
DOI: 10.1149/1.1836622
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Real‐Time Mass Spectrometric Study of the Methanol Crossover in a Direct Methanol Fuel Cell

Abstract: The products of methanol crossover through the acid‐doped polybenzimidazole polymer electrolyte membrane (PBI PEM) to the cathode of a prototype direct methanol fuel cell (DMFC) were analyzed using multipurpose electrochemical mass spectrometry (MPEMS) coupled to the cathode exhaust gas outlet. It was found that the methanol crossing over reacts almost quantitatively to CO2 at the cathode with the platinum of the cathode acting as a heterogeneous catalyst. The cathode open‐circuit potential is inversely prop… Show more

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Cited by 234 publications
(103 citation statements)
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“…For PBI membranes, the electro-osmotic drag coefficient of methanol was found to be essentially zero [207]. Similar results of the methanol crossover rate were obtained by a methanol sorption/permeation method [21] and a realtime spectrometric analysis of the cathode exhaust stream of a fuel cell operating with a current [210], indicating little contribution of the electro-osmotic drag mechanism. For PBI membranes doped with 5 mol H 3 PO 4 per repeat unit at 150 • C and 50/50 water/methanol vapour, the methanol crossover was found to be corresponding to less than 10 mA cm −2 for a 100 m thick membrane [21,210], equivalent to a methanol crossover rate of about 10 −10 mol cm −1 s −1 bar −1 .…”
Section: Electro-osmotic Water Drag and Methanol Crossoversupporting
confidence: 74%
“…For PBI membranes, the electro-osmotic drag coefficient of methanol was found to be essentially zero [207]. Similar results of the methanol crossover rate were obtained by a methanol sorption/permeation method [21] and a realtime spectrometric analysis of the cathode exhaust stream of a fuel cell operating with a current [210], indicating little contribution of the electro-osmotic drag mechanism. For PBI membranes doped with 5 mol H 3 PO 4 per repeat unit at 150 • C and 50/50 water/methanol vapour, the methanol crossover was found to be corresponding to less than 10 mA cm −2 for a 100 m thick membrane [21,210], equivalent to a methanol crossover rate of about 10 −10 mol cm −1 s −1 bar −1 .…”
Section: Electro-osmotic Water Drag and Methanol Crossoversupporting
confidence: 74%
“…Several non-fluorinated polymeric materials have been investigated as replacements for Nafion due to low cost and ease of synthesis [5][6][7][8][9][10][11][12], but they are generally based on free sulfonic acid groups and experience severe dimensional swelling in DMFC at high degree of sulfonation, resulting in mechanical instability problems [1,12,13]. Cross-linked ionomers have been pursued to overcome this problem, but they usually lead to a sacrifice in fuel cell performance and microphase-separation is easy to occur in such blends due to different, incompatible acidic (aromatic) and basic (polybenzimidazole) polymer structures [14,15].…”
Section: Introductionmentioning
confidence: 99%
“…It was expected an increase of cathode losses due to methanol crossover and consequent oxidation in the presence of oxygen and platinum [5,19,21]. Furthermore, at 180 ºC, it is expected an increase in cathode tolerance to methanol, despite the possible increase in the methanol crossover [6].…”
Section: Eismentioning
confidence: 99%
“…A high temperature DMFC was first studied in the 1990's using phosphoric acid doped PBI as electrolytes [3][4][5]. The assembled DMFC reached a maximum of 0.1 W·cm -2 , at 200 °C [4].…”
Section: Introductionmentioning
confidence: 99%