Process analysis of a liquid-feed direct methanol fuel cell system
Recently, a greatly increasing interest in solid polymer electrolyte fuel cells (PEFC) for a range of applications has been observed. The direct methanol fuel cell (DMFC) based on a PEFC uses methanol directly for electric power generation and promises technical advantages, for example, for power tr...
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Veröffentlicht in: | Journal of power sources 2000-12, Vol.91 (2), p.193-201 |
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Format: | Artikel |
Sprache: | eng |
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Zusammenfassung: | Recently, a greatly increasing interest in solid polymer electrolyte fuel cells (PEFC) for a range of applications has been observed. The direct methanol fuel cell (DMFC) based on a PEFC uses methanol directly for electric power generation and promises technical advantages, for example, for power trains.
This study analyses the interaction between a DMFC stack fed with a liquid aqueous methanol solution and the peripheral system equipment. A simulation model of a DMFC system for mobile applications (from methanol to net electricity) is presented to calculate system efficiencies on the basis of thermodynamic engineering calculations.
Based on the simulation calculations, useful operating requirements can be specified. To optimise the performance of DMFC systems, it is necessary to consider the operational characteristics of all the components required in the system. There are worldwide activities to improve the performance of a DMFC stack, which depends on numerous operating parameters. But it is not sufficient to optimise only the current/potential curves of the fuel cell without taking all the consequences for the system into consideration. The results of the computer simulation presented here emphasise the difficulties in improving fuel cell performance without decreasing system efficiency and describes the consequences for the system's operation conditions.
Priorities are additionally set concerning the heat management of the fuel cell stack. In the case of liquid fuel supply, the water crossover through the membrane and the ensuing vapourisation at the cathode side impairs the thermal balance. Key operating parameters, which influence these effects, are pressure, temperature, air flow and methanol permeation rate. |
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ISSN: | 0378-7753 1873-2755 |
DOI: | 10.1016/S0378-7753(00)00472-9 |