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Étude du reformage d'hydrocarbures liquides assisté par plasma hors-équilibre pour la production de gaz de synthèse

机译:非平衡等离子体辅助液态烃重整生产合成气的研究

摘要

The direct use of hydrogen as an energy vector currently faces difficulties due to both the lack of a distribution infrastructure, and to technical limitations concerning hydrogen storage. Before the transition to a “direct hydrogen” economy, a possible intermediate step could be the onboard hydrogen production from conventional car fuels. Non-thermal, plasma-assisted reforming provides an alternative to conventional industrial catalytic reforming, since the latter has limitations when an onboard system. The objective of this work is the characterization of plasma assisted reforming technology, through various parametric studies (factors influencing flow – geometry of the cylindrical electrode, pattern of behaviour, pressure, polarity – and factors influencing chemical conditions – initial mixture, total flow rate, injected electrical power, nature of combustible components), on both experimental and theoretical fronts. A study of the behaviour of the torch in non-reactive conditions (steam water, air) was first performed. The reforming reaction was then studied under various conditions (POx, SR, ATR), using gasoline SP95, ethanol, E85 and diesel fuel; establishing the adaptability of the reactor. A simple physical model of the arc was also developed in the case of air. The modelling of the reactor focused then on different aspects. Firstly, the study of flow showed that the good mixing between the three reactive species (air, water, octane) was attained quickly during their injection in the reactor, conferring an axial symmetry on the system. The study of a 1D kinetic model then served to highlight the role of radicals in the activation of the reaction of reforming. This was followed by a sensitivity analysis. A coupled model taking into account correlation between flow (2D axisymetric) and the reactions of chemical kinetics was finally worked out, with emphasis placed on the sequence of reactions in the reactor as a whole.
机译:由于缺乏分配基础设施以及有关储氢的技术限制,直接将氢用作能量载体目前面临困难。在过渡到“直接氢”经济之前,可能的中间步骤可能是使用常规汽车燃料生产车载氢。非热等离子体辅助重整提供了常规工业催化重整的替代方法,因为后者在车载系统中存在局限性。这项工作的目的是通过各种参数研究(影响流量的因素-圆柱电极的几何形状,行为方式,压力,极性-以及影响化学条件的因素-初始混合物,总流量,在实验和理论方面都注入了电力,可燃成分的性质)。首先进行了对火炬在非反应条件(蒸汽,空气)中的行为的研究。然后使用汽油SP95,乙醇,E85和柴油在各种条件下(POx,SR,ATR)研究重整反应;建立反应堆的适应性。在空气情况下,还开发了一个简单的电弧物理模型。然后,反应器的建模集中在不同方面。首先,流动研究表明,在将三种反应物(空气,水,辛烷)注入反应器期间,它们很快达到了良好的混合状态,使系统具有轴向对称性。然后,对一维动力学模型的研究突出了自由基在重整反应活化中的作用。随后进行敏感性分析。最终建立了一个考虑了流量(二维轴距)和化学动力学反应之间相关性的耦合模型,重点放在整个反应器中的反应顺序上。

著录项

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    Petitpas Guillaume;

  • 作者单位
  • 年度 2008
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  • 原文格式 PDF
  • 正文语种 fr
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