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Design and control of acetic acid dehydration system via heterogeneous azeotropic distillation

机译:非均相共沸乙酸脱水系统的设计与控制

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Acetic acid dehydration is an important operation in the production of aromatic acid, such as terephthalic acid or in the manufacture of cellulose acetate. Although acetic acid and water does not form azeotrope, but using simple distillation to separate these two components is not practical. The reason is because the system has tangent pinch on the pure water end, thus it is more customary in industry to use an entrainer via a heterogeneous azeotropic distillation column system for the separation. In this study, a suitable entrainer is selected from three candidate acetates through rigorous steady-state simulation of this system. Optimum process design and operating condition are determined to keep high-purity bottom acetic acid composition and also keep a small acetic acid loss through top aqueous draw. Furthermore. the overall control strategy of this column system is proposed to hold both bottom and top product specifications in spite of feed rate and feed composition load disturbances. The proposed overall control strategy is very simple requiring only one tray temperature control loop inside the heterogeneous azeotropic column. (C) 2004 Elsevier Ltd. All rights reserved.
机译:乙酸脱水在芳族酸如对苯二甲酸的生产中或在乙酸纤维素的生产中是重要的操作。尽管乙酸和水不会形成共沸物,但是使用简单的蒸馏来分离这两种成分是不切实际的。原因是因为该系统在纯水末端有切线夹角,因此在工业中更常见的是通过非均相共沸蒸馏塔系统使用夹带剂进行分离。在这项研究中,通过对该系统进行严格的稳态模拟,从三种候选乙酸盐中选择合适的夹带剂。确定最佳的工艺设计和操作条件,以保持高纯度的塔底乙酸成分,并通过塔顶含水馏分保持少量乙酸损失。此外。提出了该塔系统的总体控制策略,以在饲料速度和饲料成分负荷干扰的情况下保持产品的底部和顶部规格。所提出的总体控制策略非常简单,仅需在非均相共沸塔内部只有一个塔板温度控制回路即可。 (C)2004 Elsevier Ltd.保留所有权利。

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