Method for synthesizing thiazine ketone
A synthetic method, the technology of buprofezin, which is applied in the field of synthetic process of chemical products to achieve the effect of solving environmental protection problems
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Embodiment 1
[0021] 500L of benzene (430kg) was added to a 1000L reactor, stirred; 64.6kg of phosgene (content 80%, phosgene to N-methylaniline molar ratio of 1.4:1) was slowly introduced, and then 40kg of N-methylaniline was added dropwise. Base aniline, control the reaction temperature at 10-20°C, after the dripping, fill the phosgene until it is colorless and transparent. Add catalyst benzoyl peroxide then, pass into chlorine gas 35.2kg (the mol ratio of chlorine gas and N-methylphenylcarbamoyl chloride is 1.4: 1), sampling analysis after 1 hour, when chlorination conversion rate reaches 93% At ~97%, the chlorination reaction is complete. Connect a vacuum device to desolventize the chlorinated material under negative pressure. When the end point temperature is 100-110°C and the end point vacuum degree is ≥0.080MPa, the desolventization is completed, and 130.54kg of light yellow transparent liquid, N-chloromethyl The content of phenylcarbamoyl chloride is 45.6%, and the yield based on N...
Embodiment 2
[0023] Add 500L of chlorinated benzene (430kg) into a 1000L reactor, stir; slowly pass into phosgene 64.6kg (content 80%, phosgene and N-methylaniline molar ratio is 1.4:1), and then add dropwise 40kg of N-methylaniline, the reaction temperature is controlled at 50-60°C, after the dripping is completed, phosgene is replenished until it is colorless and transparent. Add catalyzer azobisisobutyronitrile then, pass into chlorine gas 35.2kg (the mol ratio of chlorine gas and N-methylphenylcarbamoyl chloride is 1.4: 1), sampling analysis after 1 hour, when chlorination conversion ratio reaches 93 % to 97%, the chlorination reaction is over. Connect a vacuum device to desolventize the chlorinated material under negative pressure. When the end point temperature is 120-130°C and the end point vacuum degree is ≥0.070MPa, the desolventization is completed, and 91.83kg of light yellow transparent liquid, N-chloromethyl The content of phenylcarbamoyl chloride is 65.8%, and the yield is 8...
Embodiment 3
[0025] Add 500L of chlorinated benzene (550kg) into a 1000L reactor and stir; slowly feed 74.3kg of phosgene (80% content, phosgene to N-methylaniline molar ratio of 1.3:1) and then dropwise add 50kgN -Methylaniline, the reaction temperature is controlled at 60-70°C, and after the dripping is completed, phosgene is replenished until it is colorless and transparent. Add catalyst benzoyl peroxide then, pass into chlorine gas 41kg (the mol ratio of chlorine gas and N-methylphenylcarbamoyl chloride is 1.3: 1), sampling analysis after 1 hour, when chlorination conversion rate reaches 93%~ At 97%, the chlorination reaction is over. Connect a vacuum device to desolventize the chlorinated material under negative pressure. When the end point temperature is 120-130°C and the end point vacuum degree is ≥0.075MPa, the desolventization is completed, and 160.82kg of light yellow transparent liquid is obtained, N-chloromethyl The content of phenylcarbamoyl chloride is 46.7%, and the yield b...
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