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On-board hydrogen storage for fuel cell vehicle

机译:用于燃料电池车辆的板载储氢

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Methods for onboard storage of hydrogen were evaluated for use in a fuel cell vehicle. Compressed hydrogen gas and cryogenic liquid hydrogen seem to be the two most viable options. Both these storage options were modelled, for storage of 5 kg hydrogen, to be implemented in an automotive fuel cell system simulation model. Hydrogen discharge was simulated for different values of cell stack operating pressure and temperature, using a constant rate of hydrogen release, and the power requirement for heating of the hydrogen to fuel cell stack operating temperature was calculated. The calculations show that compressed gaseous hydrogen storage requires a heating capacity of 0.72-1 kW for stack operating temperatures of 343 - 368 K. In the case of liquid hydrogen storage, heating demand for vaporisation and heating of the fuel was calculated to between 10 and 13 kW for stack operating temperatures of 343 - 368 K. The fuel cell stack produces surplus heat that can be used for fuel heating. Calculations show that the heat content of the cooling medium is sufficient to heat the fuel stream to approximately 20 K below tack temperature, with temperature differences in heat exchangers being the limiting factor. The radiator / compartment heating and humidifier will also extract heat from the cooling medium. However, to reach system temperature an auxiliary heat source will be required. This could be in the form an electrical heater or a hydrogen burner. Also, for liquid hydrogen storage, a power demand arises for maintaining operating pressure inside the storage vessel during hydrogen release. This was calculated to between 13 and 28 W for the fuel cell stack operating conditions simulated, and this power demand can be supplied by directing a stream of released and heated hydrogen through a coil running inside the storage vessel.
机译:评价氢气储存的方法用于燃料电池载体。压缩的氢气和低温液体氢似乎是最活力的选择。这两种存储选项都被建模,用于储存5千克氢,以在汽车燃料电池系统仿真模型中实现。用恒定氢释放的恒定速率模拟电池堆工作压力和温度的不同值的氢气放电,并计算加热氢气以燃料电池堆工作温度的功率要求。该计算表明,压缩的气态储氢需要0.72-1kW的加热容量,用于343-368k的堆叠工作温度。在液体储氢的情况下,将对汽化的加热和加热燃料的加热计算为10到10之间。 343 - 368 K的堆叠工作温度为13 kW。燃料电池堆产生可用于燃料加热的剩余热量。计算表明,冷却介质的热含量足以将燃料流加热至低于粘性温度的大约20 k,热交换器温度差是限制因子。散热器/隔室加热和加湿器还将从冷却介质中提取热量。然而,为了达到系统温度,将需要辅助热源。这可以是电加热器或氢燃烧器的形式。而且,对于液体储氢,出现了在氢释放期间保持储存容器内的工作压力的功率要求。这是计算到模拟燃料电池堆操作条件的13和28W,并且可以通过将释放和加热的氢气引导通过储存容器内的线圈来提供该功率需求。

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