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Experimental investigation and theoretical modeling of inhomogeneity in filter media.

机译:过滤介质不均匀性的实验研究和理论建模。

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摘要

Theoretical modeling of filter behavior is required for predicting media performance and for improving filter designs. Initial efforts to model the filtration process assumed the filter media to be homogeneous, i.e ., all fibers sized and spaced uniformly. These simplified theories are seen to be inadequate in predicting the media filtration characteristics and the inherent filter inhomogeneities have to be taken into consideration.;The deviation of the experimental filter efficiency values from the theoretical predictions are seen to be a function of the operating conditions and media type. This is not accounted for in the classical approach to model inhomogeneity. The different inhomogeneities in a media---i.e., non-uniform packing density distribution, polydisperse fiber diameters, and three-dimensional fiber structure---must be taken into consideration in developing a filter model for inhomogeneous media.;The packing densities in a commercial filter media are seen to be non-uniformly distributed. These variations in packing density affect the local velocities and hence the filtration characteristics. A filter scanner has been built to study the effect of packing density variations on local filter efficiencies as a function of the operating conditions. The particle counts are obtained over small regions of a filter and the count distribution is obtained by translating the filter along the different directions. Based on the observed packing density distributions, a simplistic statistical theoretical model is developed. The effect of the packing density distribution on local velocity and efficiency distributions are obtained and the total efficiency of a inhomogeneous media is calculated based on the filter macroscale properties.;The fiber drag values and a monodisperse estimate of the fiber diameter distribution in the filter are required for use with the theoretical model. The inhomogeneity in the media result in experimental fiber drag values lower than the theoretical predictions. To obtain an accurate estimate of the filter fiber drag, an asymmetric three-dimensional model is developed. The fiber drag values are calculated as a function of the inter-fiber distance ratio, packing density distribution and fiber diameter polydispersity.;These fiber drag values are seen to be closer to the experimental predictions for real filter media. A drag-equivalent fiber diameter is defined based on the calculated fiber drag expressions and measured pressure drop values. Comparisons with experimental results indicate that the calculated diameter values are close to the experimental observations.;The calculated fiber drag and drag-equivalent fiber diameter values are used with the statistical theoretical model to obtain the distribution of local efficiencies. The total filter efficiency values are then calculated and seen to correlate well with the total efficiency measurements of the different media.
机译:需要使用过滤器行为的理论模型来预测介质性能和改进过滤器设计。对过滤过程进行建模的最初尝试是假设过滤介质是均匀的,即所有纤维的大小和间距均一。这些简化的理论被认为不足以预测介质的过滤特性,必须考虑固有的过滤器不均匀性;实验过滤器效率值与理论预测值的偏差被认为是运行条件的函数,并且媒体类型。在经典的非均质模型方法中没有考虑到这一点。在开发非均匀介质的过滤器模型时,必须考虑介质中不同的不均匀性,即不均匀的堆积密度分布,多分散纤维直径和三维纤维结构。商业过滤介质被认为是不均匀分布的。堆积密度的这些变化会影响局部速度,进而影响过滤特性。已经建立了过滤器扫描仪,以研究填充密度变化对局部过滤器效率的影响,该影响取决于操作条件。粒子计数是在滤镜的小区域上获得的,而计数分布是通过沿不同方向平移滤镜获得的。基于观察到的堆积密度分布,建立了简单的统计理论模型。获得了堆积密度分布对局部速度和效率分布的影响,并根据过滤器的宏观特性计算了不均匀介质的总效率。纤维阻力值和过滤器中纤维直径分布的单分散估计为需要与理论模型一起使用。介质中的不均匀性导致实验纤维阻力值低于理论预测值。为了获得对过滤纤维阻力的准确估计,建立了一个不对称的三维模型。计算纤维阻力值是纤维间距离比,堆积密度分布和纤维直径多分散性的函数。这些纤维阻力值被认为更接近于实际过滤介质的实验预测。基于计算出的纤维阻力表达式和测得的压降值定义等效纤维的直径。与实验结果的比较表明,计算出的直径值接近于实验观察值。所计算出的纤维阻力和等效纤维直径与统计理论模型一起用于获得局部效率的分布。然后计算出总过滤器效率值,并认为该值与不同介质的总效率测量值具有很好的相关性。

著录项

  • 作者

    Dhaniyala, Suresh.;

  • 作者单位

    University of Minnesota.;

  • 授予单位 University of Minnesota.;
  • 学科 Applied Mechanics.;Engineering Mechanical.
  • 学位 Ph.D.
  • 年度 1998
  • 页码 183 p.
  • 总页数 183
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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