Energy-saving and environmental-protection butyl acrylate production method
A technology of butyl acrylate and production method, which is applied in the separation/purification of carboxylate, preparation of carboxylate, chemical instruments and methods, etc. It can solve the problems of difficult polymer treatment and excessive waste water, and achieve the service life of solid alkali The effects of long life, saving steam, and reducing the probability of side reactions
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[0017] Example 1
[0018] Such as figure 1 As shown, the energy-saving and environmentally-friendly production method of butyl acrylate of this embodiment 1 adopts continuous feeding. The raw material acrylic acid and n-butanol are fed in at a molar ratio of 1:1, and the methyl sulfonic acid catalyst is directly added to the esterification. In the kettle, the total feed is 1800L / h. After the raw materials are heated, the esterification reaction is carried out in the esterification kettle. The temperature of the esterification kettle is 95℃~96℃, and the pressure is 32kpa~38kpa. Keep the tower kettle circulating flow around 1300L / h, and the reboiler temperature around 93°C. After the reaction, the product undergoes azeotropic distillation, and the azeotrope enters the esterification tower in binary and ternary forms for separation. The top temperature of the esterification tower is about 68°C and the pressure is about 25kpa. The top distillate of the esterification tower is conde...
Example Embodiment
[0021] Example 2
[0022] Such as figure 1 As shown, the energy-saving and environmentally-friendly production method of butyl acrylate of this embodiment 2 adopts continuous feeding, and the raw material acrylic acid and n-butanol are added at a molar ratio of 1:1.1, and the methyl sulfonic acid catalyst is directly added to the esterification In the kettle, the total feed is 2500L / h. After the raw materials are heated, the esterification reaction is carried out in the esterification kettle. The temperature of the esterification kettle is 97°C~98°C and the pressure is 32kpa~38kpa. Keep the tower kettle circulating flow rate of the esterification kettle at about 2000L / h, and the reboiler temperature at about 99°C. After the reaction, the product undergoes azeotropic distillation, and the azeotrope enters the esterification tower in binary and ternary forms for separation. The top temperature of the tower is about 69°C and the pressure is about 25kpa. The overhead distillate o...
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