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Pervaporation membrane module design.

机译:渗透汽化膜模块设计。

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Pervaporation is a separation process in which a liquid mixture contacts a selective membrane. Some of the liquid evaporates across the membrane. A vacuum pump or an inert gas sweep then removes this vapor from the other side of the membrane. Finally, it is collected by a condenser. This process has selectivity not only from evaporation but also from the membrane. Thus, extremely high selectivities are possible.; Our research has been in three main areas: flat sheet membrane modules, lumen flow hollow fiber modules, and external flow hollow fiber modules.; We conducted pervaporation experiments on flat sheet modules to gain property data for a polydimethylsiloxane (PDMS) membrane separating chloroform from water. These experiments gave us the ideal separation as well as the permeability of chloroform in PDMS. This permeability turns out to be concentration dependent.; We experimented with several different lumen flow hollow fiber designs, measuring their performance. By varying the liquid velocity, we measured the membrane resistance and the liquid boundary layer resistance. Using the flat sheet results with nitrogen permeability, we calculated a membrane resistance, finding it to be similar to the measured value. We found a correlation for the boundary layer resistance of lumen flow in the transitional region from laminar to turbulent that is reproducible although differing from other mass transfer results.; External flow, however, offers greater potential for small boundary layers. We constructed an external flow module using baffles to direct the liquid flow back and forth across the fibers as it flowed down the module, since cross flow offers the best mass transfer. We characterized the performance of this design, finding it to be dominated by cross flow mass transfer, which agrees with other heat and mass transfer experiments.; We also carried out experiments evaluating the effect of vapor resistance on separation. We looked at both the location of vacuum and the addition sweep to the vacuum. We found that, even under extreme conditions, these had no effect. We concluded that the vapor side resistance is negligible.; We examined the effect of polydispersity mathematically. Polydispersity reflects the fact that hollow fibers in a module differ from one another. We analyzed several forms of diameter variation between fibers finding it to reduce the performance of the module. Coating thickness variation could either improve or hinder the performance depending on conditions. We found that diameter variation within one fiber improves the performance.; From this research we suggested the optimal design and operating parameters for pervaporative VOC remediation.
机译:全蒸发是一种分离过程,其中液体混合物与选择性膜接触。一些液体在整个膜上蒸发。然后用真空泵或惰性气体吹扫从膜的另一侧除去该蒸气。最后,由冷凝器收集。该过程不仅对蒸发具有选择性,而且对膜具有选择性。因此,极高的选择性是可能的。我们的研究主要集中在三个方面:平板膜组件,流明中空纤维组件和外流中空纤维组件。我们在平板模块上进行了全蒸发实验,以获取将氯仿与水分离的聚二甲基硅氧烷(PDMS)膜的性能数据。这些实验为我们提供了理想的分离效果以及氯仿在PDMS中的渗透性。事实证明,这种渗透率与浓度有关。我们尝试了几种不同的流明中空纤维设计,以测量其性能。通过改变液体速度,我们测量了膜电阻和液体边界层电阻。使用具有氮渗透性的平板结果,我们计算了膜电阻,发现它与测量值相似。我们发现,从层流到湍流过渡区域的管腔流动边界层阻力的相关性是可重现的,尽管与其他传质结果有所不同。但是,外部流动为较小的边界层提供了更大的潜力。我们使用折流板构造了一个外部流动模块,以使液体沿着模块向下流动时,在纤维之间来回流动,因为交叉流动提供了最佳的质量传递。我们对这种设计的性能进行了表征,发现它受到错流传质的支配,这与其他传热和传质实验一致。我们还进行了评估耐蒸气性对分离效果的实验。我们同时查看了真空的位置和扫除真空的位置。我们发现,即使在极端条件下,这些也没有作用。我们得出的结论是,蒸气侧阻力可以忽略不计。我们用数学方法检查了多分散性的影响。多分散性反映了一个事实,即组件中的中空纤维彼此不同。我们分析了纤维之间直径变化的几种形式,发现它们降低了组件的性能。取决于条件,涂层厚度的变化可能会改善或阻碍性能。我们发现一根光纤内的直径变化可以改善性能。通过这项研究,我们提出了用于全挥发VOC修复的最佳设计和操作参数。

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