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Geometric Description of the Soot Cake in a One-Dimensional Model of an Octo-Square Asymmetric Particulate Filter

机译:辛开型不对称颗粒过滤器一维模型中烟灰饼的几何描述

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Asymmetric particulate filters (PF), where the inlet channel is wider than the outlet channel, are commonly used because of their greater ash capacity. Surprisingly, very few models for asymmetric PFs have been published. This paper considers how to model the soot cake in octo-square asymmetric PFs. Some previous studies have neglected the octahedral shape of the inlet channel and instead assumed that the inlet channels were square. As the correct approach for modelling the soot cake is not obvious, three options are considered. The calculation of soot-loaded channel perimeter and hydraulic diameter (which are important for heat and mass transfer), soot thickness and backpressure as a function of soot loading are given for each geometry. In option 1, the shape of the soot-loaded channel is assumed to be geometrically similar to the soot-free channel. This is the simplest option mathematically, but results in the soot cake being thicker over the slanted sides of the inlet channel than over the straight sides (for the normal case where the straight sides are longer than the slanted sides), resulting in non-uniform flow which complicates calculation of backpressure and soot oxidation rate. Options 2 and 3 avoid such complications. Option 2 assumes that gas only passes through the straight sides of the inlet channel, resulting in the soot building up along the straight sides only. With option 3, the thickness of the soot cake is the same over the straight and slanted sides with gas leaving the channels through both straight and slanted sides. Predictions for option 2 are significantly different from those of options 1 and 3, which are quite similar. Literature data (CFD, microscopy), suggest against option 2. Therefore, option 1 is favoured as it gives comparable results to the seemingly more correct option 3, but is much simpler to code.
机译:不对称微粒过滤器(PF),其中入口通道比出口通道宽,通常是由于其较大的灰分能力而使用。令人惊讶的是,已经发布了很少有非对称PFS模型。本文考虑如何在八大方的不对称PFS中模拟烟灰饼。一些以前的研究忽略了入口通道的八面体形状,而是假设入口通道是正方形。由于烟灰饼的正确方法不明显,考虑了三种选择。每个几何形状给出,给出了作为烟灰加载的函数的烟灰加载通道周边和液压直径(这对于热量和传质),烟灰厚度和背压是重要的。在选项1中,假设烟灰加载通道的形状是几何上类似于无烟烟道的通道。这是数学上最简单的选择,但是导致烟灰饼上的入口通道的倾斜侧比在直线上(对于直边长于倾斜侧的正常情况),导致不均匀复杂化合物和烟灰氧化率计算的流动。选项2和3避免此类并发症。选项2假设气体仅通过入口通道的直线,导致仅沿直线构建的烟灰。通过选件3,烟灰滤饼的厚度在直线和倾斜的侧面上是相同的,气体通过直线和倾斜的侧面离开通道。选项2的预测与选项1和3的预测显着不同,它们非常相似。文献数据(CFD,显微镜),建议反对选项2.因此,选项1是有利的,因为它给出了看似更正确的选项3的可比结果,但要更简单到代码。

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