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The ethanol oxidation reaction and product distributions in a direct ethanol fuel cell

机译:乙醇氧化反应和直接乙醇燃料电池中的产物分布

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摘要

A novel online system for quantifying product distributions of ethanol oxidation in direct ethanol fuel cells was developed. This system was shown to have many advantages over previously reported methodologies such as: ease of operation, quick response time, economical, and real time analysis. This system consisted of a non-dispersive infrared CO₂ detector coupled with a flow-through conductivity detector for CO₂ and acetic acid measurements, respectively. The third ethanol oxidation product, acetaldehyde, was shown to be accurately calculated using a Faradaic charge balance. -- The effects of fuel and product crossover were closely examined. It was shown that the use of oxygen at the cathode can lead to an overestimation of ethanol oxidation products, mainly acetic acid, due to ethanol crossing through the membrane and reacting chemically with oxygen at the cathode. Furthermore, it was shown that significant amounts of acetaldehyde produced during ethanol oxidation were lost due to crossover, leading to an underestimation of its yield. To obtain more accurate product distributions, the fuel cell was operated using N₂/H₂ gas at the cathode (which eliminated the chemically oxidized ethanol reaction). To further improve the accuracy of product yields, a “crossover mode” approach to operating a fuel cell was examined. It was found that this method increased selectivity towards complete oxidation (carbon dioxide) by reducing poisoning of the electrode. -- A kinetic and mechanistic study on the ethanol oxidation reaction was also carried out using an electrode stripping technique. It was found that applying a potential in the range where CO is oxidized, followed by allowing the cell to return to open circuit and then re-applying the potential led to significant increases in CO₂ yields. It was found that the CO₂ yield was dependent on the length of the pulse applied, the shorter the pulsing interval, the higher the yield. This suggests that the majority of the CO₂ produced was attributed to the oxidation of CO adsorbates. The time interval between pulses was also examined. It was found that the CO₂ yield was independent of the resting time, suggesting a rapid dissociation of ethanol on the electrode, which supports previous Iiterature findings. -- A Pt-RuSnO₂/C anode catalyst was developed and tested in our system. This catalyst was found to increase both the performance and the selectivity towards CO₂ in comparison to a Pt electrode, which is rarely reported in the literature.
机译:开发了一种新颖的在线系统,用于定量直接乙醇燃料电池中乙醇氧化产物的分布。与以前报道的方法相比,该系统具有许多优势,例如:操作简便,响应时间短,经济和实时分析。该系统由一个非分散式红外CO 2检测器和一个流通电导率检测器组成,分别用于测量CO 2和乙酸。使用法拉第电荷平衡可准确计算出第三种乙醇氧化产物乙醛。 -仔细检查了燃料和产品交叉的影响。结果表明,由于乙醇穿过膜并在阴极与氧气发生化学反应,因此在阴极使用氧气会导致对乙醇氧化产物(主要是乙酸)的高估。此外,显示出由于交叉反应,乙醇氧化过程中产生的大量乙醛损失了,导致其产率低估。为了获得更准确的产品分布,燃料电池在阴极使用N 2 / H 2气体运行(这消除了化学氧化的乙醇反应)。为了进一步提高产品产量的准确性,研究了一种用于运行燃料电池的“交叉模式”方法。已发现该方法通过减少电极的中毒而增加了对完全氧化(二氧化碳)的选择性。 -还使用电极剥离技术进行了乙醇氧化反应的动力学和机理研究。已经发现,在CO被氧化的范围内施加电势,然后使电池返回开路,然后重新施加电势导致CO 2产率的显着增加。已经发现,CO 2的产率取决于所施加的脉冲的长度,脉冲间隔越短,产率就越高。这表明产生的大部分CO 2归因于CO吸附物的氧化。还检查了脉冲之间的时间间隔。已经发现,CO 2的产量与静置时间无关,表明乙醇在电极上迅速解离,这支持了以前的Iertature的发现。 -开发了Pt-RuSnO2 / C阳极催化剂并在我们的系统中进行了测试。与Pt电极相比,发现该催化剂可提高性能和对CO 2的选择性,这在文献中很少报道。

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    James David D.;

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  • 年度 2013
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