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    Effect of Channel Depth and Cell Temperature on the Performance of a Direct Methanol Fuel Cell

    Source: Journal of Fuel Cell Science and Technology:;2013:;volume( 010 ):;issue: 003::page 31002
    Author:
    Alizadeh, Ebrahim
    ,
    Farhadi, Mousa
    ,
    Sedighi, Kurosh
    ,
    Shakeri, Mohsen
    DOI: 10.1115/1.4024151
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: The 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.
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      Effect of Channel Depth and Cell Temperature on the Performance of a Direct Methanol Fuel Cell

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    contributor authorAlizadeh, Ebrahim
    contributor authorFarhadi, Mousa
    contributor authorSedighi, Kurosh
    contributor authorShakeri, Mohsen
    date accessioned2017-05-09T00:59:25Z
    date available2017-05-09T00:59:25Z
    date issued2013
    identifier issn2381-6872
    identifier otherfc_10_3_031002.pdf
    identifier urihttp://yetl.yabesh.ir/yetl/handle/yetl/151988
    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.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleEffect of Channel Depth and Cell Temperature on the Performance of a Direct Methanol Fuel Cell
    typeJournal Paper
    journal volume10
    journal issue3
    journal titleJournal of Fuel Cell Science and Technology
    identifier doi10.1115/1.4024151
    journal fristpage31002
    journal lastpage31002
    identifier eissn2381-6910
    treeJournal of Fuel Cell Science and Technology:;2013:;volume( 010 ):;issue: 003
    contenttypeFulltext
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