2017
DOI: 10.1016/j.jprocont.2017.06.014
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Highly integrated direct methanol fuel cell systems minimizing fuel loss with dynamic concentration control for portable applications

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Cited by 7 publications
(4 citation statements)
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“…In many applications, w P might not be a simple constant and the objective might not depend linearly on efficiency and power density (cf. Equations (12) and (13)). Via w P , not only technical but also nontechnical design objectives, like economic, ecological, social or political factors, can be coupled into the design process.…”
Section: General Design Considerationsmentioning
confidence: 99%
See 1 more Smart Citation
“…In many applications, w P might not be a simple constant and the objective might not depend linearly on efficiency and power density (cf. Equations (12) and (13)). Via w P , not only technical but also nontechnical design objectives, like economic, ecological, social or political factors, can be coupled into the design process.…”
Section: General Design Considerationsmentioning
confidence: 99%
“…Robustness to the strongly changing environmental conditions, especially temperature and humidity of air inlet, are furthermore crucial. Model-based analysis allows a systematic evaluation and quantification of effects of environmental conditions [11] and of process integration for weight minimisation [12]. Assessing the wide range of system design options is out of scope of this work; instead, the fuel cell is designed in the context of the whole system.…”
Section: Introductionmentioning
confidence: 99%
“…Furthermore, robustness to the strongly changing environmental conditions, especially temperature and humidity of the inlet air is crucial. The model-based analysis allows a systematic evaluation and quantification of the effects of environmental conditions (Zenith et al, 2010) and process integration for weight minimization (Na et al, 2017).…”
Section: Introductionmentioning
confidence: 99%
“…Their results indicated that 98% of the water from the cathode outlet must be recycled at an average cell voltage of 0.33 V and a cell temperature 62 °C. An alternative approach for modeling a DMFC system was developed by Na et al [22]. They focused on reducing the high amount of methanol loss due to evaporation in the separator and mixer.…”
Section: Introductionmentioning
confidence: 99%