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1.A shortcut design using the Fenske Underwood Gilliland(FUG) equations of continuous distillation design is developed based on the reasonable approximation that the batch distillation column can be considered as a continuous distillation column with changing feed The method is a powerful and computationally fast tool that can be used in batch vacuum distillation process design
对间歇真空精馏过程的近似处理,将一个间歇真空精馏过程看作是一个改变进料组成的拟稳态连续过程,从而用于连续过程设计的Fenske-Underwood-Gililand方程被应用到间歇真空精馏过程的设计计算。 该简捷设计法对组份较多且未知的复杂体系的间歇真空精馏过程的初步设计是适宜的。收藏指正
2.Thus, the method has overcome the shortcomings of Underwood formula, and provides a sound basis for short-cut design of multicomponent batch distillation column.
方法并不要求相对挥发度为常数 ,并且能准确计算顶浓 ,克服了通常所采用的Underwood公式法的缺陷 ,为多元分批精馏的简捷设计奠定了基础 .收藏指正
3.The design strategies proposed were applied to design the distillation column for ideal and non-ideal multicomponent systems and the result shows that the stage composition lines method is better than Fenske-Underwood shortcut method and conforms to the simulation results of Aspen plus.
对理想和非理想物系进行的实例研究结果表明,由塔板组成线设计法得到的计算结果优于Fenske-Underwood简捷法,与Aspenplus的模拟结果吻合较好。收藏指正