Method for removing by-product dimethyl sulfide in moxidectin production process
A technology for the production process of dimethyl sulfide, applied in the field of eliminating the by-product dimethyl sulfide in the production process of moxictine, can solve the problems of low boiling point, nasal irritation, flammability, etc., and achieve the absorption process Simple, optimized production environment, low cost of raw materials
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Embodiment 1
[0027] Dissolving nimoctine in the reaction solvent methylene chloride, then adding the acid-binding agent triethylamine and the upper protection reagent 4-chlorophenoxyacetyl chloride, fully stirring until the end of the reaction, adding excess water to quench the reaction solution, Separate the oil layer, obtain the nimoctine with protective group through drying and precipitating, combine it with activated dimethyl sulfoxide reagent (dimethyl sulfoxide / phenyl dichlorophosphate), acid-binding agent triethylamine and the solvent dichloromethane used in the oxidation step are mixed for oxidation reaction. After reaching the end point of the reaction, an excessive amount of water is added to quench the oxidation reaction solution, and then a nitrogen blowing precipitation device is connected, and the nitrogen flow rate is controlled at 30mL / min. Control at 25-30°C, and control the temperature of the absorption tank and condenser with 50g of sodium hypochlorite solution (5 times t...
Embodiment 2
[0029] Dissolving nimoctine in the reaction solvent methylene chloride, then adding the acid-binding agent triethylamine and the upper protection reagent 4-chlorophenoxyacetyl chloride, fully stirring until the end of the reaction, adding excess water to quench the reaction solution, Separate the oil layer, obtain the nimoctine with protective group through drying and precipitating, combine it with activated dimethyl sulfoxide reagent (dimethyl sulfoxide / phenyl dichlorophosphate), acid-binding agent triethylamine And the solvent dichloromethane used in the oxidation step is mixed to carry out the oxidation reaction. After reaching the end of the reaction, add excess water to quench the oxidation reaction solution, and then connect to the nitrogen blowing precipitation device. The nitrogen flow rate is controlled at 300mL / min. Control at 18-22°C, and control the temperature of the absorption kettle and condenser with 150g of sodium hypochlorite solution (7 times the amount of th...
Embodiment 3
[0031]Dissolving nimoctine in the reaction solvent methylene chloride, then adding the acid-binding agent triethylamine and the upper protection reagent 4-chlorophenoxyacetyl chloride, fully stirring until the end of the reaction, adding excess water to quench the reaction solution, Separate the oil layer, obtain the nimoctine with protective group through drying and precipitating, combine it with activated dimethyl sulfoxide reagent (dimethyl sulfoxide / phenyl dichlorophosphate), acid-binding agent triethylamine and the solvent methylene chloride used in the oxidation step are mixed for oxidation reaction. After reaching the end of the reaction, excess water is added to quench the oxidation reaction solution, and then connected to a negative pressure precipitation device. The temperature of the oxidation reaction kettle is controlled at 25-30 ° C. The temperature of the absorption kettle and condenser with 100g of sodium hypochlorite solution is controlled at 0-5°C, and then he...
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