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Dehydration of Acetic Acid by Azeotropic Distillation in the Production of Aromatic Acids (Azeotropic Distillation in the Production of an Aromatic Acid)

机译:芳香酸生产中的共沸蒸馏法脱水乙酸(芳香酸生产中的共沸蒸馏法)

摘要

In a process for preparing an aromatic dicarboxylic acid such as terephthalic acid by liquid phase oxidation of its precursor (e.g. p-xylene), an overhead stream 10 comprising an aqueous aliphatic carboxylic acid is added to the column 12 ). / RTI The azeotropic distillation can be carried out using a reflux of the entaluminous solo (22) with little or no entrainer and with controlled entrainment of the entrainer to obtain a base product (34) containing a predetermined amount of residual water . Any aromatic dicarboxylic acid precursor present in the overhead stream is separated from the aliphatic dicarboxylic acid by removal at position 24 near the entry point of the feed 10 introduced into the column. The amount of water in the bottom product 34 may be controlled by the adjustment of a separate water feed 76 to the lower region of the azeotropic distillation column. In addition, an adjustment of the reflux rate (via line 22) may be used to control the water content in the bottom product and to maintain column operation upon loss of feed to the column.
机译:在通过其前体(例如对二甲苯)的液相氧化制备芳族二羧酸例如对苯二甲酸的方法中,将包含水性脂族羧酸的塔顶料流10添加到塔12中。共沸蒸馏可使用含铝单质(22)的回流在几乎没有夹带剂或没有夹带剂的情况下进行,并在夹带剂的受控夹带下进行,以获得含有预定量的残留水的基础产物(34)。通过在引入塔中的进料10的入口点附近的位置24处除去,将塔顶物流中存在的任何芳族二羧酸前体与脂族二羧酸分离。底部产物34中的水量可以通过将分离的水进料76调节至共沸蒸馏塔的下部区域来控制。另外,可以使用回流速率的调节(通过管线22)来控制塔底产物中的水含量,并在损失进入塔的进料时保持塔的运行。

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