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Azeotropic Distillation Process with Vertical Divided-Wall Column

机译:垂直分隔壁塔的共沸蒸馏工艺

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In order to separate a homogeneous binary azeotropic mixture, such as thanol and water, into individual components, an entrainer is usually added to form a new heterogeneous ternaryazeotropic mixture. An azeotropic distillation method with the conventional two-column sequence is usually used to complete the separation task. In this paper, we present a new azeotropic distillattion column with a vertical di dividing wall, developed by improving the divided-wall column for ordinary three-component mixture separation as reported by Wright. The new system differs greatly from the conventional two-column sequence. In this sysem, the column is equidpped with one condenser at the top and two reboilers at the bottom, allowing single-column azeotropic distillation. The features of this column are demonstrated by simulation for ethanol dehydration using cyclohexane as entrainer in comparison with the conventional two-column system. It is confirmed that for dehydration of a 90 wt% ethanol feed stock, an energy saving of about 7% can be expected.
机译:为了将均相的二元共沸混合物(例如三醇和水)分离为单独的成分,通常需要添加夹带剂以形成新的异质三元共沸混合物。通常使用具有常规两塔顺序的共沸蒸馏方法来完成分离任务。在本文中,我们提出了一种新型的具有垂直分隔壁的共沸蒸馏塔,该色谱柱是通过改进分隔壁塔来开发的,以实现常规的三组分混合物分离(如Wright所报道)。新系统与常规的两列顺序有很大不同。在该系统中,该塔的顶部装有一个冷凝器,底部装有两个再沸器,可进行单塔共沸蒸馏。与常规的两塔系统相比,通过使用环己烷作为夹带剂对乙醇脱水进行模拟,证明了该色谱柱的功能。已经证实,对于90wt%的乙醇原料的脱水,可以预期节省约7%的能量。

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