Numerical simulation of the performance of air-breathing direct formic acid microfluidic fuel cells

This work numerically investigated the effects of various factors on the performance of air-breathing direct formic acid microfluidic fuel cells. An MFC with a microchannel width of 1.5 mm, depth of 0.05 mm, and electrode spacing of 0.3 mm was used in the simulation. An MFC which was a 1.5-mm-wide,...

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Published inMicro & nano letters Vol. 12; no. 11; pp. 860 - 865
Main Authors Herlambang, Yusuf Dewantoro, Shyu, Jin-Cherng, Lee, Shun-Ching
Format Journal Article
LanguageEnglish
Published Stevenage The Institution of Engineering and Technology 01.11.2017
John Wiley & Sons, Inc
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ISSN1750-0443
1750-0443
DOI10.1049/mnl.2017.0322

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Summary:This work numerically investigated the effects of various factors on the performance of air-breathing direct formic acid microfluidic fuel cells. An MFC with a microchannel width of 1.5 mm, depth of 0.05 mm, and electrode spacing of 0.3 mm was used in the simulation. An MFC which was a 1.5-mm-wide, 0.05-mm-deep microchannel installed with two 0.3-mm-apart electrodes was used in the simulation. The mixture of formic acid at concentrations of 0.3, 0.5, and 1.0 M and 0.5-M sulphuric acid served as fuel, while a 0.5-M sulphuric acid stream served as the electrolyte introduced at inlet flow rates of 0.05, 0.1, and 0.5 mL/min. First, a three-dimensional MFC model was built using COMSOL Multiphysics 5.1 to simulate the fuel cell performance. Subsequently, I–V curves obtained from simulations and from published experimental data under similar operating conditions were compared to ensure the validity of the simulation. Transport phenomena were formulated with a continuity equation, momentum equation, species transport equation, and charge equation. Additionally, the flow through porous media in the gas diffusion layer was described using the Brinkman equation, whereas the Butler–Volmer equation was applied to obtain I–V and P–I curves. The current density distribution resulting from internal current loss and reactant concentration on both electrodes was also determined in this work.
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ISSN:1750-0443
1750-0443
DOI:10.1049/mnl.2017.0322