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Understanding the effects of internal air bleed, nitrogen dilution, and sulfur dioxide on the performance of PEM fuel cells.

机译:了解内部排气,氮气稀释和二氧化硫对PEM燃料电池性能的影响。

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Data are presented to quantify how oxygen diffusing across the catalyst coated membrane (CCM) from the cathode side affects the performance of a PEMFC operating with low levels of CO in H2. The extent of CO poisoning, as measured by the anode overpotential was decreased when the cathode backpressure was increased from 101 to 303 kPa and when the CCM thickness was decreased from 25 mum to 5 mum. The data indicate that a lowering of the anode overpotential for 50, 100, and 500 ppm CO in H2 by the O2 diffusing through the membrane is a complicated function of CCM thickness, adsorption isotherms of H2, CO, and apparent rate constant of CO with O2. Under relatively high anode overpotential, the reaction of Ru-OH with adsorbed CO was the primary means of CO oxidation and the diffusing O2 reacts with H2. However, at cell voltage close to open circuit conditions, the O2 reacting with CO is kinetically limited. The diffused oxygen (also known as internal air bleed) was quantified with a model that includes O2 solubility and heterogeneous oxidation constants. The results indicate that the surface reaction of Pt-O and Pt-CO limits the effect of internal air bleed for thin CCMs.; Data are shown here that can be used to quantify the competition between CO and H2 adsorption on CCMs during PEMFC operation. These data are based on experiments with N2 dilution and this dilution might be expected due to H2 is consumed down the length of the channel or reformate concentration changes. The specific data are reported to examine the N2 dilution effect on CO poisoning. These data indicate, as expected, that the effect of CO poisoning is more pronounced when H2 is diluted at constant CO concentration. The unusual observation and the one that shows competitive CO/H2 adsorption for the first time in PEMFC literature is that the extent of poisoning (as measured by the anode polarization) is also more pronounced as H2 is diluted with N 2 even though the ratio of CO/H2 is held constant. Thus it is shown that the presence of N2 not only dilutes H2 but also makes the adsorbed CO more difficult to desorb from the surface of the anode catalyst.; The last part of this dissertation focuses on an air impurity SO 2. Transient data of SO2 in air are presented and an empirical relationship between cathode polarization loss and the concentration and dosage in mumole of SO2 in air was developed for the PRIMEA Series 56 CCM from W. L. Gore & Associates Inc. This relationship and the data are used to suggest a poisoning mechanism for SO2 in air and a mathematical model. Thus the transient behavior was modeled for the various SO2 concentrations and the model predictions based on the proposed poisoning mechanism was shown to agree with the experimental data very well. The goal is to present a methodology that aids the industry in their quest to characterize concentration and dosage effects on PEMFC performance. Experimentally this characterization is initiated by systematically decreasing the SO2 concentration from high levels to low levels approaching nominally low concentrations in unfiltered cathode feeds.
机译:呈现数据以量化从阴极侧扩散穿过整个催化剂涂层膜(CCM)的氧气如何影响在H2中CO含量低的PEMFC的性能。当阴极背压从101 kPa增加到303 kPa以及CCM厚度从25 mum减小到5 mum时,通过阳极过电势测量的CO中毒程度降低。数据表明,通过膜中扩散的O2降低H2中50、100和500 ppm CO的阳极过电势是CCM厚度,H2,CO的吸附等温线以及CO的表观速率常数的复杂函数。氧气在较高的阳极超电势下,Ru-OH与吸附的CO的反应是CO氧化的主要手段,而扩散的O2与H2反应。但是,在接近开路条件的电池电压下,与CO反应的O2在动力学上受到限制。使用包括O2溶解度和非均相氧化常数的模型对扩散的氧气(也称为内部排气)进行定量。结果表明,Pt-O和Pt-CO的表面反应限制了薄CCM的内部放气效果。此处显示的数据可用于量化PEMFC操作期间CCM上CO和H2吸附之间的竞争。这些数据是基于使用N2稀释的实验得出的,由于在通道长度或重整产品浓度变化的情况下会消耗掉H2,因此可以预期这种稀释。报道了具体数据以检查N2稀释对CO中毒的影响。如预期的,这些数据表明,当以恒定的CO浓度稀释H2时,CO中毒的影响更加明显。不寻常的观察结果和在PEMFC文献中首次显示出竞争性的CO / H2吸附的观察结果是,即使H2被N 2稀释,中毒程度(通过阳极极化测量)也更加明显,因为H2被N 2稀释。 CO / H2保持恒定。因此表明,N 2的存在不仅稀释了H 2,而且使吸附的CO更难以从阳极催化剂的表面脱附。本文的最后一部分着眼于空气中的SO 2杂质。给出了空气中SO2的瞬态数据,并开发了PRIMEA系列56 CCM的阴极极化损耗与空气中SO2的浓度和剂量之间的经验关系。 WL Gore&Associates Inc.此关系和数据用于建议空气中SO2的中毒机理和数学模型。因此,对各种SO2浓度的瞬态行为进行了建模,并且基于所提出的中毒机理的模型预测表明与实验数据非常吻合。目的是提出一种可帮助行业寻求表征浓度和剂量对PEMFC性能影响的方法。实验上,通过系统地将SO2浓度从高水平降低到接近未过滤阴极进料中名义上的低浓度的低水平来启动此表征。

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