A kind of preparation method of 2,4-dichlorobenzonitrile
A technology of dichlorobenzonitrile and dichlorobenzyl alcohol, which is applied in the field of preparation of 2,4-dichlorobenzonitrile, can solve the problems of high comprehensive cost, reduce production cost, improve product quality, and avoid the use of metal catalysts Effect
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Embodiment 1
[0019] Add magneton, 2mL glacial acetic acid, 0.5mmol 2,4-dichlorobenzyl alcohol, 1.5mmol ammonium acetate, 0.15mmol nitric acid and 0.15mmol tetramethylpiperidine nitrogen oxide into the glass reaction tube in sequence (the pressure of oxygen is 1atm ). After the reaction test tube was sealed, it was put into a heating tank at 50° C., and reacted for 12 hours under magnetic stirring. Once the reaction time was reached, the reaction system was cooled to room temperature, and the product was subjected to internal standard quantitative analysis by gas chromatography, and the yield of 2,4-dichlorobenzonitrile product was obtained as 93%. Then the above experiment was repeated, and the product was separated and purified by column chromatography to obtain 2,4-dichlorobenzonitrile product. use 1 H-NMR, 13 C-NMR confirmed the product structure see figure 1 and 2 .
Embodiment 2
[0021] Add magnetite, 2 mL of glacial acetic acid, 0.5 mmol of 2,4-dichlorobenzyl alcohol, 1.5 mmol of ammonium acetate, 0.15 mmol of nitric acid, and 0.15 mmol of tetramethylpiperidine nitroxide into a glass-lined autoclave in sequence. After the reaction kettle was sealed, it was filled with 10atm oxygen, placed in a heating tank at 50°C, and reacted for 12 hours under magnetic stirring. Once the reaction time was reached, the reaction system was cooled to room temperature, and the internal standard quantitative analysis of the product was carried out by gas chromatography, and the yield of 2,4-dichlorobenzonitrile product was obtained as 77%.
Embodiment 3-4
[0023] The ammonium acetate in Example 1 was changed to ammonium sulfate and ammonium nitrate, and other conditions were unchanged, so that the yield of the product (gas-phase internal standard) was 63%, 52%, respectively.
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