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Modeling of liquid and air transport processes within a filtering mist separator

机译:过滤雾分离器内的液体和空运过程建模

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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 (=holdup) 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:液体和空气中液体和空气的处理的描述是对过滤特异性性质的研究(压降,分离效率......)的基本基础。对于雾分离器,已经在微观水平上进行了详细的研究以了解单纤维上的液滴沉积和运动。然而,由于纤维的复杂布置(随机取向,接触点的未知数量为......),那些方程的应用通常由于纤维的复杂布置而导致的宏观水平往往失败。首先,通过简单的动态系统建模过滤雾分离器内的空气和液体运输的复杂过程。假设系统内的空气和液体质量(= HOLDUP)直接相互依赖并引起流动进出。这些传输流由公式描述,该公式是简单的等式,包括用于不同传输机构的参数(空气传输,重力,粘合力)。此外,系统中的空气和液体含量用于估计不同的所得过滤特异性特性(例如压降)。将开发的公式施加在二维细胞网格上,这简化了复杂的真实过滤介质。对于每个细胞,通过逐步计算空气和液体流量来计算空气和液体堆积,直到达到稳定状态。将液体储量和压降演变的仿真结果与真正的线/玻璃纤维过滤器的实验结果进行了比较。因此,测试显示过滤器的压降仍然增加了一段时间,尽管已经实现了一定的恒定液体储存。通过检查过滤器的模拟液体持续曲线,可以对压降增加的解释。发现液体通过过滤器移动并在滤光器清洁气体侧堆积,这导致空气阻力的增加,分别增加了压降。

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