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Modeling of liquid and airtransport processes within a filtering mist separator

机译:过滤雾分离器内液体和空气传输过程的建模

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Description of transport processes of liquid and air within a filtering mist separator is an essential basis for investigations of filtration specific properties (pressure drop, separation efficiency ...). For mist separators there have already been detailed studies at microscopic level to understand the droplet deposition and movement on a single fiber. The application of those equations to macroscopic level, for example an entire filter, however, often fails due to the complex arrangement of the fibers (random orientation, unknown numbers of contact points...).On a first basis the complex processes of air and liquid transport within a filtering mist separator were modeled by a simple dynamic system. It was assumed that air and liquid masses (=ho!dup) within a system depend directly on each other and cause flows in and out. These transport flows were described by formulas which are simple equations including parameters for different transport mechanism (air transport, gravity, adhesive force). The air and liquid holdups in the system were furthermore used to estimate different resulting filtration specific properties (e.g. pressure drop).The developed formulas were applied on a 2-dimensional cell grid, which simplifies a complex real filter medium. For each cell the air and liquid holdup was calculated by a stepwise calculation of air and liquid flow values until a steady state was reached. Simulation results of the evolution of the liquid holdup and pressure drop were compared to experimental results of a real wire/glass-fiber filter. Thereby the tests revealed that the pressure drop of the filter still increased for some time although a certain constant liquid holdup already had been achieved. An explanation for that increase of the pressure drop could be made by the examination of the simulated liquid holdup profile of the filter. It was found out that the liquid is moving through the filter and is piling up at the filters clean gas side which causes an increase of the air resistance, respectively an increase of the pressure drop.
机译:描述液体和空气在过滤雾分离器内的传输过程是研究过滤特性(压降,分离效率...)的必要基础。对于雾气分离器,已经在微观层面进行了详细的研究,以了解液滴在单根纤维上的沉积和运动。但是,由于纤维的复杂排列(随机取向,接触点的数目未知...),这些等式在宏观层面(例如整个过滤器)的应用通常会失败。一个简单的动态系统对过滤雾分离器内的液体和液体的传输进行了建模。假定系统内​​的空气和液体质量(= houpup)直接相互依赖,并导致流入和流出。这些输送流用简单的公式来描述,这些公式包括用于不同输送机制(空气输送,重力,粘附力)的参数。此外,系统中的空气和液体滞留量还用于估算不同的最终过滤特性(例如压降)。将已开发的公式应用于二维单元格,可简化复杂的实际过滤介质。对于每个单元,通过逐步计算空气和液体流量值直至达到稳态,来计算空气和液体的滞留率。将液体滞留量和压降演变的模拟结果与真实的金属丝/玻璃纤维过滤器的实验结果进行了比较。由此测试表明,尽管已经实现了一定的恒定持液量,但过滤器的压降仍会增加一段时间。可以通过检查过滤器的模拟液体滞留曲线来解释压降的增加。已经发现,液体正在流过过滤器,并在过滤器的清洁气体侧堆积,这导致空气阻力的增加或压降的增加。

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