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Evaluation of the experimental model for methanol crossover in DMFCs
Independent transport measurements of carbon dioxide permeation were undertaken to evaluate a standard assumption of attributing cathodic CO2 flux in direct methanol fuel cells (DMFCs) entirely to methanol crossover. With a humid air cathode at ambient conditions, a DMFC cathode emanated 3.5 to 4 x...
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Published in: | Journal of the Electrochemical Society 2004, Vol.151 (3), p.A413-A417 |
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container_end_page | A417 |
container_issue | 3 |
container_start_page | A413 |
container_title | Journal of the Electrochemical Society |
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creator | DRAKE, Javit A WILSON, William KILLEEN, Kevin |
description | Independent transport measurements of carbon dioxide permeation were undertaken to evaluate a standard assumption of attributing cathodic CO2 flux in direct methanol fuel cells (DMFCs) entirely to methanol crossover. With a humid air cathode at ambient conditions, a DMFC cathode emanated 3.5 to 4 x 10-8 mol/(cm2 s) of CO2 (20 to 25 mA/cm2 'leak current density'). From a methanol-free anode feed of either carbonated liquid water or humid CO2 /H2 gas (90%: 10%), carbon dioxide permeated to the cathode at 0.7 x 10-8 mol/(cm2 s) or 20% of the total DMFC flux. Under current (enabled with the presence of H2 in CO2), the permeation rate rose to 1 x 10-8 mol/(cm2 s). The rise with cell current density increase from 24 to 80 mA/cm2 was quantitatively consistent with convection of CO2 with electro-osmosis of water. The indication that anodic CO2 contributes to the total cathodic flux has a positive implication for fuel efficiency in DMFCs. |
doi_str_mv | 10.1149/1.1646150 |
format | article |
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With a humid air cathode at ambient conditions, a DMFC cathode emanated 3.5 to 4 x 10-8 mol/(cm2 s) of CO2 (20 to 25 mA/cm2 'leak current density'). From a methanol-free anode feed of either carbonated liquid water or humid CO2 /H2 gas (90%: 10%), carbon dioxide permeated to the cathode at 0.7 x 10-8 mol/(cm2 s) or 20% of the total DMFC flux. Under current (enabled with the presence of H2 in CO2), the permeation rate rose to 1 x 10-8 mol/(cm2 s). The rise with cell current density increase from 24 to 80 mA/cm2 was quantitatively consistent with convection of CO2 with electro-osmosis of water. 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With a humid air cathode at ambient conditions, a DMFC cathode emanated 3.5 to 4 x 10-8 mol/(cm2 s) of CO2 (20 to 25 mA/cm2 'leak current density'). From a methanol-free anode feed of either carbonated liquid water or humid CO2 /H2 gas (90%: 10%), carbon dioxide permeated to the cathode at 0.7 x 10-8 mol/(cm2 s) or 20% of the total DMFC flux. Under current (enabled with the presence of H2 in CO2), the permeation rate rose to 1 x 10-8 mol/(cm2 s). The rise with cell current density increase from 24 to 80 mA/cm2 was quantitatively consistent with convection of CO2 with electro-osmosis of water. The indication that anodic CO2 contributes to the total cathodic flux has a positive implication for fuel efficiency in DMFCs.</description><subject>Applied sciences</subject><subject>Energy</subject><subject>Energy. 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Thermal use of fuels</topic><topic>Equipments for energy generation and conversion: thermal, electrical, mechanical energy, etc</topic><topic>Exact sciences and technology</topic><topic>Fuel cells</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>DRAKE, Javit A</creatorcontrib><creatorcontrib>WILSON, William</creatorcontrib><creatorcontrib>KILLEEN, Kevin</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Technology Research Database</collection><collection>Aerospace Database</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Electronics & Communications Abstracts</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Engineering Research Database</collection><jtitle>Journal of the Electrochemical Society</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>DRAKE, Javit A</au><au>WILSON, William</au><au>KILLEEN, Kevin</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Evaluation of the experimental model for methanol crossover in DMFCs</atitle><jtitle>Journal of the Electrochemical Society</jtitle><date>2004</date><risdate>2004</risdate><volume>151</volume><issue>3</issue><spage>A413</spage><epage>A417</epage><pages>A413-A417</pages><issn>0013-4651</issn><eissn>1945-7111</eissn><coden>JESOAN</coden><abstract>Independent transport measurements of carbon dioxide permeation were undertaken to evaluate a standard assumption of attributing cathodic CO2 flux in direct methanol fuel cells (DMFCs) entirely to methanol crossover. With a humid air cathode at ambient conditions, a DMFC cathode emanated 3.5 to 4 x 10-8 mol/(cm2 s) of CO2 (20 to 25 mA/cm2 'leak current density'). From a methanol-free anode feed of either carbonated liquid water or humid CO2 /H2 gas (90%: 10%), carbon dioxide permeated to the cathode at 0.7 x 10-8 mol/(cm2 s) or 20% of the total DMFC flux. Under current (enabled with the presence of H2 in CO2), the permeation rate rose to 1 x 10-8 mol/(cm2 s). The rise with cell current density increase from 24 to 80 mA/cm2 was quantitatively consistent with convection of CO2 with electro-osmosis of water. The indication that anodic CO2 contributes to the total cathodic flux has a positive implication for fuel efficiency in DMFCs.</abstract><cop>Pennington, NJ</cop><pub>Electrochemical Society</pub><doi>10.1149/1.1646150</doi></addata></record> |
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subjects | Applied sciences Energy Energy. Thermal use of fuels Equipments for energy generation and conversion: thermal, electrical, mechanical energy, etc Exact sciences and technology Fuel cells |
title | Evaluation of the experimental model for methanol crossover in DMFCs |
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