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Titlebook: Control of Fuel Cell Power Systems; Principles, Modeling Jay T. Pukrushpan,Anna G. Stefanopoulou,Huei Peng Book 2004 Springer-Verlag London

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Natur und Freiheit im Denken Kantsn models. A block diagram of the stack model is shown in Figure 3.1. A stack thermal submodel can be added in the future when temperature changes are taken into account. The electrochemical reaction happening at the membranes is assumed to occur instantaneously. In this model, the stack temperature
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https://doi.org/10.1007/978-3-658-40949-4gement [1]. We assume here a perfect air/fuel flow humidifier, and coolers for the incoming air and the stack. These perfect conditions are implemented in the simulation model by either fixing appropriate variables or by employing simple static controllers described in the previous chapter. Moreover
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Vermessung digitaler Arbeitsweltentions, fueling the fuel cell system using natural gas is often preferred because of its wide availability and extended distribution system [36]. Common methods of converting natural gas to hydrogen include steam reforming and partial oxidation. The most common method, steam reforming, which is endot
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Control of Fuel Cell Power Systems978-1-4471-3792-4Series ISSN 1430-9491 Series E-ISSN 2193-1577
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https://doi.org/10.1007/978-3-658-41057-5tarvation or wasted hydrogen [79] and (ii) maintain a desired temperature of the CPDX catalyst bed for high conversion efficiency [91]. Accurate control and coordination of the fuel processor reactant flows can prevent both large deviation of hydrogen concentration in the anode and large excursion of the CPDX catalyst bed temperature.
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Jay T. Pukrushpan,Anna G. Stefanopoulou,Huei PengShows the reader the latest research in the control of fuel cell technology, this will contribute to the commercial viability of the technology.The authors’ background in automotive technology gives t
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