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Gas Phase Simulation of an Ethanol Autothermal Reforming Reactor for Hydrogen Production for Fuel Cell Vehicles

机译:燃料电池氢生产乙醇自热再热反应器的气相模拟

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Hydrogen fuel cell technology is currently capable of providing adequate power for a wide range of stationary and mobile applications. Nonetheless, the sustainability of this technology rests upon the production of hydrogen from renewable resources. Among the techniques under current study, the chemical reforming of alcohols and other bio-hydrocarbon fuels, appears to offer great promise. In the so called autothermal reforming process, a suitable combination of total and partial oxidation supports hydrogen production from ethanol with no external addition of energy required. Furthermore, the autothermal reforming process conducted in a well insulated reactor, spawns temperatures that promote additional hydrogen production through the endothermic steam reforming and the water-gas shift reactions, which may be catalyzed or uncatalyzed, with the added benefit of lowered carbon monoxide concentrations. In this study, an adiabatic ethanol reforming reactor was simulated assuming the reactants to be air (21% O_2 and 79% N_2) and ethanol (C_2H_5OH) and the products to be H_2O, CO_2, CO and H_2, with all constituents taken to be in the gaseous state. The air was introduced uniformly through a ring around the side of the reactor and the gaseous ethanol was injected into the center of one end, with products withdrawn from the center of the opposite end, to create an axisymmetric flow field. The gas flows within the reactor were assumed to be turbulent, and the chemical kinetics of a simple four reaction system was assumed to be controlled by turbulent mixing processes. Air and fuel flow rates into the reactor were varied to obtain six different levels of oxidation (air-fuel ratios) while maintaining the same total gaseous mass flow out of the reactor. The numerical results for the reacting flow show that hydrogen production is maximized when the air-fuel ratio on a mass basis is held at approximately 2.8. These findings are in qualitative agreement with observations from previous experimental studies.
机译:氢燃料电池技术目前能够为各种固定式和移动应用提供足够的动力。尽管如此,该技术的可持续性依赖于可再生资源的氢气生产。在目前研究的技术中,醇和其他生物烃燃料的化学改造似乎提供了很大的承诺。在所谓的自热重整过程中,总和部分氧化的合适组合支持来自乙醇的氢气,不需要外部添加能量。此外,在绝缘反应器中进行的自热重整过程,产生通过吸热蒸汽重整和水性气体移反应的促进额外氢气产生的温度,其可以催化或未催化,具有降低的一氧化碳浓度的增加的益处。在该研究中,假设反应物是空气(21%O_2和79%N_2)和乙醇(C_2H_5OH)和作为H_2O,CO_2,CO和H_2的产物的所有成分所带来的所有成分所带来的所有成分,模拟了绝热乙醇重整反应器。在气态状态。通过围绕反应器侧的环均匀地引入空气,并将气态乙醇注入一端的中心,用来自相对端的中心取出的产物,以产生轴对称流场。假设反应器内的气体流动是湍流的,并且假设简单的四种反应系统的化学动力学被湍流混合方法控制。在反应器中变化空气和燃料流速,以获得六种不同水平的氧化(空气燃料比),同时保持相同的总气体质量流出反应器。反应流动的数值结果表明,当质量的空燃比保持在约2.8时,氢产生最大化。这些发现与先前实验研究的观察结果进行了定性协议。

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