A scheme of a fuel feeding sub-section in a direct hydrogen FCS for automotive application is shown in Fig. 4.2. Pressure regulation sub-system design has the objective to regulate inlet pressure to assure the hydrogen flow rate necessary to the chemical reaction. The inlet pressure and fuel purge represent the main parameters to be controlled in both operative modes, however, the role of the purge valve is different for the two possible configurations. In a dead-end configuration and when air is used as oxidant, nitrogen tends to crossover from the cathode flow field through the electrolyte to the anode side. As fuel is consumed in the fuel cell, the concentration of nitrogen in the anode compartment increases, thus accumulating therein and negatively impacting the performance of the fuelcell [5]. Moreover, the humidification control (see Sect. 4.5) could create operativephases characterized by a dangerous stagnation of liquid droplets on surface ofelectrodes in cathode and anode sides, favoring flooding of the compartments andfuel starvation, and then interfering with the access of the hydrogen fuel duringstack power requirement. Then the purge action, draining out the possible excessof nitrogen and water accumulated in anode compartment, can eliminate most ofliquid molecules from the catalyst surface and refresh the feed. As a consequencethe overall strategy for maintaining the well-hydrated cell membranes, assuring areliable and efficient stack operation with minimization of nitrogen crossover andsimultaneously avoiding the flooding phenomena, should involve the periodicacting of the purge valve. This is normally closed but, when necessary, the controlstrategy expects to open it by managing the opening frequency for a specifiedopening time, sufficient to drain the contaminants but not too long for undesiredleaking of useful fuel. In order to evaluate the effect of purge operation on FCSefficiency, it is possible to define a coefficient expressing the ratio of fuelconverted to fuel supplied (gutil in Sect. 6.2), which can reach values higher than90% in optimized realizations [6, 7].
图4.2显示了用于汽车的直接氢FCS中的燃料进料子区示意图。压力调节子系统设计的目的是调节入口压力,以确保化学反应所需的氢气流速。进气压力和燃油净化是两种操作模式下要控制的主要参数,但是,对于两种可能的配置,净化阀的作用是不同的。在无用配置中,当将空气用作氧化剂时,氮趋于从阴极流场穿过电解质流到阳极侧。随着燃料在燃料电池中的消耗,阳极室中的氮浓度增加,从而在其中积聚并负面影响燃料的性能。<br>cell [5]. Moreover, the humidification control (see Sect. 4.5) could create operative<br>phases characterized by a dangerous stagnation of liquid droplets on surface of<br>electrodes in cathode and anode sides, favoring flooding of the compartments and<br>fuel starvation, and then interfering with the access of the hydrogen fuel during<br>stack power requirement. Then the purge action, draining out the possible excess<br>of nitrogen and water accumulated in anode compartment, can eliminate most of<br>liquid molecules from the catalyst surface and refresh the feed. As a consequence<br>the overall strategy for maintaining the well-hydrated cell membranes, assuring a<br>reliable and efficient stack operation with minimization of nitrogen crossover and<br>同时避免溢流现象,应涉及放<br>气阀的周期性作用。它通常是关闭的,但在必要时,控制<br>策略希望通过在指定的<br>打开时间内管理打开频率来打开它,该时间足以排出污染物,但对于不希望<br>的有用燃料泄漏来说,时间不要太长。为了评估吹扫操作对FCS <br>效率的影响,可以定义一个系数,该系数表示<br>转化为供油的燃料的比例(第6.2节中的gutil),<br>在优化实现中该值可以达到90%以上[6]。 ,7]。
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