The solution procedure for batch distillation simulation is described in detailed.

详细描述了间歇精馏模拟计算的完整求解过程.

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We present two kinds of optimal control policy for multicomponent batch distillation.

多元间歇精馏塔最常用的操作方式是控制回流比.

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The advantages of heterogeneous batch distillation proccess make it widely used in separation of systems azeotrope.

非均相间歇共沸精馏广泛地应用于共沸物系的分离.

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The study has laid the foundation for short cut design of multicomponent batch distillation column.

该研究结果分批精馏塔的简捷设计奠定了基础.

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