'/> Numerical study of natural gas reforming by non-catalytic partial oxidation based on the Virtuhcon Benchmark
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Numerical study of natural gas reforming by non-catalytic partial oxidation based on the Virtuhcon Benchmark

机译:基于Virtuhcon基准的非催化部分氧化天然气重整的数值研究

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Graphical abstract Display Omitted Highlights ? Numerical study of non-catalytic natural gas reforming under HT/HP conditions. ? Validation of the numerical results against semi-industrial test plant experiments. ? Comparison of EDC and FPV approaches for turbulence-chemistry interaction modeling. ? The models applicability was discussed in terms of flame and reactor characteristics. Abstract The non-catalytic reforming of natural gas to syngas was studied numerically. The numerical simulations focused on the Virtuhcon Benchmark, which is a set of experimental data based on the semi-industrial scale test plant HP POX (high-pressure partial oxidation). The experimental data comprises reactor characteristics such as product gas composition and wall temperatures across the reactor for temperatures between 1473 and 1673K and pressures between 50 and 70bar(g), and optically estimated flame characteristics such as flame length and width. For turbulence-chemistry interactions, the widely used Eddy Dissipation Concept model and an advanced Flamelet/Progress-variable-based approach developed for POX processes were applied. Contrary to standard Flamelet approaches, the advanced model can describe correctly both the reaction zone and the comparatively slow chemical processes in the almost homogeneous post-flame zone. Based on the experimental data, the applicability of the different numerical models will be discussed carefully. In contrast to several literature work, the model evaluation is based not only on global reactor characteristics, but also on optical flame analyses from inside of the semi-industrial test plant, which allows to evaluate the capability of the numerical model to predict local reactive flow effects inside industrial HP/HT processes. The results reveal that both approaches allow a reliable prediction of the syngas composition, flame length, and flame width. With respect to the outlet temperature, the Eddy Dissipation Concept tends to overpredict the resulting temperature, or, from a different point of view, to underpredi
机译:<![cdata [ 图形摘要 显示省略 亮点 HT / HP条件下的非催化天然气重整的数值研究。 validati.对半工业试验厂实验的数值结果。 EDC和FPV方法的比较湍流 - 化学交互建模。 在火焰和反应堆特征方面讨论了模型的适用性。 抽象 在数值上研究了天然气对合成气的非催化重整。该数值模拟专注于Virtuhcon基准,这是一组基于半工业规模试验厂HP POX(高压部分氧化)的实验数据。实验数据包括反应器特性,例如产物气体组合物和反应器的壁温度,用于1473和1673之间的温度 k和50至70之间的压力棒(g),光学估计的火焰特性,如火焰长度和宽度。对于湍流 - 化学相互作用,应用广泛使用的涡流耗散概念模型和用于痘毒工艺开发的基于先进的火焰/进度 - 基于基于的方法。与标准的爆炸方法相反,先进的模型可以正确描述反应区和几乎均匀的火焰区域中的相对慢的化学过程。基于实验数据,将仔细讨论不同数值模型的适用性。与多个文献作品相比,模型评估不仅基于全局反应器特性,而且还基于半工业试验设备内部的光火焰分析,这允许评估数值模型的能力来预测局部反应流动的能力工业HP / HT过程内的影响。结果表明,两种方法都允许可靠地预测合成气组成,火焰长度和火焰宽度。关于出口温度,涡流耗散概念倾向于过度估计所得温度,或从不同的观点来看到欠款

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