Method for coproducing methylbenzoic acid, methyl benzonitrie and phthalonitrile
A technology of methyl benzoic acid and methyl benzonitrile, which is applied in chemical instruments and methods, purification/separation of carboxylic acid nitrile, preparation of carboxylate, etc. The problem of low yield and other problems can be avoided, and the effect of avoiding rectification residue, reducing the amount of three wastes and improving the yield is achieved.
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[0100] Example 1
[0101] The catalyst dissolved in the fresh p-xylene added to the oxidation reactor is cobalt naphthenate, metal phthalocyanine (R 1 =CH 3 CH 2 , R 2 =H, M=Mn), metalloporphyrin (R 1 =R 2 =H, R 3 =CH 3 , M=Cu) mixture, the total concentration is 75ppm, the reaction temperature is 180°C, the reaction pressure is 2MPa, and the oxygen-containing gas is oxygen-enriched air with an oxygen concentration of 24%. The conversion rate of xylene was 42%, and the oxidation reaction solution was obtained. At this time, the mass percentage content of each component in the reaction solution obtained by HPLC analysis is listed in Table 1. In the primary distillation tower, all components whose boiling point is lower than p-toluidine in the oxidation reaction liquid are rectified and separated, and the rectification is stopped when the content of p-toluidine in the still of the initial distillation tower reaches 0.06wt%, The low boiling point component is obtained at ...
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[0103] Example 2
[0104] The catalyst dissolved in the fresh paraxylene added to the oxidation reactor is MnO 2 and cobalt acetylacetonate, the total concentration is 350ppm, the reaction temperature is 150 ° C, the reaction pressure is 1MPa, the oxygen-containing gas concentration is 21%, the operation process is the same as that of Example 1, the difference is that the conversion rate of p-xylene is controlled to be 50% , the mass percentage content of p-methylbenzyl alcohol in the tower still liquid of the primary steaming tower is controlled to be 0.07%. The mass percentage composition of each component in the reaction solution obtained by HPLC analysis is listed in table 1, and the content of the toluic acid in the obtained preliminary distillation tower tower still liquid, composition and the preliminary distillation tower overhead mixture are listed in the table 2.
[0105] The above-mentioned primary distillation tower still liquid is added to the rectifying tower f...
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[0106] Example 3
[0107] The catalysts dissolved in the fresh p-xylene added to the oxidation reactor are N-hydroxyphthalimide, cobalt isooctanoate, metal phthalocyanine (R) having the structure of general formula (IV). 1 =OH, R 2 =H, M=Ru) and metalloporphyrins (R 1 =R 3 =H,R 2 =OH, M 1 =M 2 =Mn) mixture, total concentration is 10000ppm, reaction temperature is 116 ℃, reaction pressure is 0.2MPa, oxygen-containing gas is pure oxygen, operation process is identical with embodiment 1, and difference is that the transformation efficiency of p-xylene is controlled as 60%, and the mass percentage content of p-methylbenzyl alcohol in the tower still liquid of the primary steaming tower is controlled to be 0.10%. The mass percentage composition of each component in the reaction solution obtained by HPLC analysis is listed in table 1, and the content of the toluic acid in the obtained preliminary distillation tower tower still liquid, composition and the preliminary distillati...
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