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dc.contributor.authorAlizadeh, Ebrahim
dc.contributor.authorFarhadi, Mousa
dc.contributor.authorSedighi, Kurosh
dc.contributor.authorShakeri, Mohsen
dc.date.accessioned2017-05-09T00:59:25Z
dc.date.available2017-05-09T00:59:25Z
dc.date.issued2013
dc.identifier.issn2381-6872
dc.identifier.otherfc_10_3_031002.pdf
dc.identifier.urihttp://yetl.yabesh.ir/yetl/handle/yetl/151988
dc.description.abstractThe main goal of this study is to analyze the performance of the direct methanol single cell using three channel depths at various cell temperatures. The membrane electrode assembly (MEA) used Nafionآ® 117, by loading a PtRu (4 mg/cm2) catalyst at the anode and Ptblack (4 mg/cm2) catalyst at the cathode. The active area of the MEA was 100 cm (Jung et al., 2009, “Investigation of Flow Bed Design in Direct Methanol Fuel Cell,â€‌ J. Solid State Electrochem., 13, pp. 1455–1465). In these sets of experiments, anode and cathode channel depth were varied simultaneously. The cell performance is improved with an increase of temperature in a certain range because the conductivity of the membrane and the reaction kinetics at both the anode and cathode are increased. Also, when the channel depth of the bipolar plate is decreased from 2.0 to 1.0 mm, the cell performance increases. The decreased channel depth leads to an increase in the linear velocity of reactants and products.
dc.publisherThe American Society of Mechanical Engineers (ASME)
dc.titleEffect of Channel Depth and Cell Temperature on the Performance of a Direct Methanol Fuel Cell
dc.typeJournal Paper
dc.journal.volume10
dc.journal.issue3
dc.journal.titleJournal of Fuel Cell Science and Technology
dc.identifier.doi10.1115/1.4024151
dc.journal.fristpage31002
dc.journal.lastpage31002
dc.identifier.eissn2381-6910
dc.treeJournal of Fuel Cell Science and Technology:;2013:;volume( 010 ):;issue: 003
dc.contenttypeFulltext


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