Method used for preparing isophthaloyl dichloride and paraphthaloyl chloride
A technology of terephthaloyl chloride and terephthalic acid, which is applied in the field of preparation of iso/terephthaloyl chloride, can solve the problems not mentioned in the production of iso/terephthaloyl chloride, and achieve the effect of increasing the reaction rate
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Embodiment 1
[0017] (1) Put m / terephthalic acid, catalyst and thionyl chloride into the reaction kettle for reaction, put dry nitrogen into the reaction kettle by bubbling, and gradually increase the input amount of dry nitrogen as the reaction proceeds ;The reaction temperature is 70°C, the reaction pressure is -0.02Mpa, and the nitrogen gas flow rate is 50-500L / h;
[0018] (2) After the reaction, continue to feed nitrogen gas, the amount of nitrogen gas feeding is 5-200L / h, the solvent is removed from the material, the temperature is 90°C during the solvent removal, the vacuum degree is not lower than 650mmHg, and the product is refined.
Embodiment 2
[0020] (1) Put m / terephthalic acid, catalyst and thionyl chloride into the reaction kettle for reaction, put dry nitrogen into the reaction kettle by bubbling, and gradually increase the input amount of dry nitrogen as the reaction proceeds ;The reaction temperature is 100°C, the reaction pressure is 0.02Mpa, and the nitrogen gas flow rate is 50-500L / h;
[0021] (2) After the reaction, continue to feed nitrogen gas, the amount of nitrogen gas feeding is 5-200L / h, remove the solvent from the material, the temperature is 130°C during the solvent removal, the vacuum degree is not lower than 650mmHg, and the product is refined.
Embodiment 3
[0023] (1) Put m / terephthalic acid, catalyst and thionyl chloride into the reaction kettle for reaction, put dry nitrogen into the reaction kettle by bubbling, and gradually increase the input amount of dry nitrogen as the reaction proceeds ;The reaction temperature is 80°C, the reaction pressure is 0.01Mpa, and the nitrogen feed rate is 50-500L / h;
[0024] (2) After the reaction, continue to feed nitrogen gas, the amount of nitrogen gas feeding is 5-200L / h, and the solvent is removed from the material. The temperature is 100°C during the solvent removal, and the vacuum degree is not lower than 650mmHg, and it is refined to obtain.
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