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Modeling and Simulation of a Hybrid Process (Pervaporation+Distillation)using MATLAB

机译:使用MATLAB的混合过程(全蒸发+蒸馏)的建模和仿真

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This paper reports the modeling and simulation of a hybrid process, based on the combination of distillation and pervaporation, for the separation of azeotropic mixture of alcohol and ether. Pervaporation has emerged as one of the most active areas in the membrane research, and the pervaporation process has been shown to be an indispensable component for chemical separations. Pervaporation is more suitable for the separation of azeotropic or constant boiling mixtures which otherwise are difficult to separate by ordinary distillation. Although distillation is the most widely used technique for the separation of liquid mixtures, however the distillation separation of the mixtures with an azeotropic composition or close boiling mixtures is energetically expensive. A hybrid process exploits the advantages of pervaporation and distillation, while the negative aspects are minimized. Simulation tasks were carried out with MATLAB and the results of alternative process configurations that result from the relative location of separation technologies have been compared on the basis of the required membrane area.
机译:本文报道了基于蒸馏和全蒸发相结合的分离醇和醚共沸混合物的混合过程的建模和仿真。渗透蒸发已成为膜研究中最活跃的领域之一,渗透蒸发过程已被证明是化学分离必不可少的组成部分。全蒸发更适于分离共沸或恒沸混合物,否则共沸混合物或恒沸混合物很难通过常规蒸馏分离。尽管蒸馏是分离液体混合物最广泛使用的技术,但是具有共沸组合物的混合物或接近沸腾的混合物的蒸馏分离在能源上是昂贵的。混合工艺利用了全蒸发和蒸馏的优势,同时最大程度地减少了负面影响。使用MATLAB进行了仿真任务,并根据所需的膜面积比较了分离技术的相对位置所产生的替代工艺配置的结果。

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