Method for preparing propylene glycol monomethyl ether acetate (PMA) by continuous reaction and distillation
A production method and reactive distillation technology, which are applied in the field of continuous reactive distillation to prepare propylene glycol methyl ether acetate, can solve the problems of long reaction time, high material consumption and energy consumption, complicated operation and the like, and achieve the reduction of equipment corrosion rate and acetic acid mono Consumption, the effect of convenient process operation
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[0025] Raw materials PM and acetic acid are prepared in a molar ratio of 1:1 and fully mixed in the 1-raw material tank. The raw materials enter the 2-fixed-bed reactor for preliminary esterification reaction, and the fixed-bed reaction is heated by external circulation. The fixed bed reaction temperature is controlled at 70-80°C. The catalyst used is a sulfonic strong acid cation exchange resin X with macromolecular structure. The circulation ratio used by the fixed bed is R=3-5. The pre-reaction discharge material enters the esterification kettle, and the reaction temperature of the kettle is controlled at 110-140°C. The design of the esterification tank allows the reaction materials to be fully mixed while prolonging the residence time. The catalyst used in the esterification tank is methanesulfonic acid, and the catalyst consumption is 1.5w% of the tank liquid. The crude reaction product enters the bottom of the esterification tower after being heated and vaporized. Aft...
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