Method for preparing two products of polymer grade terephthalic acid and isophthalic acid from mixed aromatic hydrocarbons
A technology of terephthalic acid and isophthalic acid, which is applied in chemical instruments and methods, preparation of organic compounds, preparation of carboxylate, etc., can solve the problem of inability to use polyester raw materials, low product purity, and inability to crystallize in water phase. To achieve high-efficiency separation and other issues, to achieve the effect of improving market competitiveness and reducing separation costs
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Embodiment 1
[0035] The method provided by the present invention is used to process mixed aromatic xylene raw materials with a PX / MX ratio of 1:1 to produce two products, PTA and PIA. The organic solvent NN dimethylformamide is used for PTA purification, and the process flow is as described in the specific implementation. The process conditions of each unit equipment are listed as follows:
[0036] Table 1 Process parameters of oxidation reactor 101
[0037]
[0038] Table 2 Process parameters of oxidation reactor 102
[0039]
[0040] Table 3 Process parameters of hydrogenation reactor 201
[0041]
[0042] Table 4 Process parameters of water phase high temperature crystallization unit 301
[0043]
[0044] Table 5 Process parameters of water phase high temperature crystallization unit 302
[0045]
[0046] Table 6 Process parameters of organic solvent dissolution and recrystallization 401~402
[0047]
[0048] Table 7 Process parameters of water phase low temperature crystallizer 501
[0049]
Embodiment 2
[0051] The method provided by the present invention is used to process mixed aromatic xylene raw materials with a PX / MX ratio of 1:1 to produce two products, PTA and PIA. The organic solvent N-methylpyrrolidone is used for PTA purification, and the process flow is as described in the specific embodiment The conditions of oxidation, hydrogenation and high-temperature water crystallization are the same as those in Example 1. The purity and process parameters of the product obtained by dissolving in organic solvent and low-temperature crystallization are as follows:
[0052] Table 8 Process parameters of organic solvent dissolution and recrystallization 401~402
[0053]
[0054] Table 9 Process parameters of water phase low temperature crystallizer 501
[0055]
[0056] Compared with Example 1, the ability of using N-methylpyrrolidone to dissolve terephthalic acid is stronger in Example 2 and the complete dissolution of crude TA can be achieved with less solvent and lower temperature, b...
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