Method for treating acetic acid and water containing dialkylaromatics by azeotropic distillation
A technology of dialkylaromatics and azeotropic distillation, which is applied in chemical instruments and methods, preparation of carboxylate, preparation of organic compounds, etc., can solve the problems of difficult operation, increased investment cost, increased condenser and online analysis Instrument and other problems, to achieve the effect of simple operation, low cost, and reduce the content of organic matter
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Embodiment 1
[0037] A feed stream 1 of acetic acid and water containing p-xylene enters the azeotropic distillation column A from the 14th tray at a flow rate of 5075.71kg / h, and the concentration of acetic acid in the feed stream 1 is 54.6wt% , the p-xylene flow rate is 13.6kg / h, and the azeotropic distillation column is 45 trays. Simultaneously, a stream 6 is continuously drawn out at the position side of the 10th plate of the lower limit of the p-xylene enrichment (azeotropic region) of the azeotropic rectification tower, and its extraction amount is close to the flow rate of p-xylene in the feed stream 1, That is 15.92kg / h. according to figure 2 It can be seen from the temperature distribution that the temperature here is about 96.3°C, and the corresponding components in stream 6 are p-xylene concentration of 47.5wt%, sec-butyl acetate concentration of 19.1wt%, water concentration of 19.6wt%, acetic acid Concentration 12wt% and methyl acetate 1.8wt%. In the present invention, the s...
Embodiment 2
[0040] A feed stream 1 of acetic acid and water containing p-xylene enters the azeotropic distillation column A from the 22nd tray at a flow rate of 5075.71kg / h, and the concentration of acetic acid in the feed stream 1 is 74.6wt% , the p-xylene flow rate is 13.6kg / h, and the azeotropic distillation column is 45 trays. Simultaneously, a stream 6 is continuously drawn out at the side of the 18th plate plate position of the lower limit of the p-xylene enrichment (azeotropic region) of the azeotropic rectification tower, and its extraction amount is close to the flow rate of p-xylene in the feed stream 1, That is 14.62kg / h. according to figure 2 It can be seen from the temperature distribution that the temperature here is about 98.6°C, and the corresponding components in stream 6 are the concentration of p-xylene 40.5wt%, the concentration of sec-butyl acetate 23.1wt%, the concentration of water 21.6wt%, and the concentration of acetic acid 12.5wt% and methyl acetate 2.3wt%. ...
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