Energy-saving method for preparing isopropyl acetate
A technology of isopropyl acetate and methyl acetate, applied in the field of chemical reaction engineering, can solve the problems of long post-treatment process, shortened reaction process, accumulation of olefin oligomers, etc.
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Embodiment 1
[0023] Attached figure 1 As shown in the process flow, the pressurized reaction distillation column C1 is a plate tower with a diameter of 700 mm and a height of 30 meters, with 50 trays inside; among them, there are 9 plates in the rectification section, 36 plates in the reaction section, and 5 plates in the stripping section. plate. The operating pressure is 3atm, the operating reflux ratio is 2.3, the temperature of the bottom of the tower is 126-128°C, and the temperature of the top of the tower is 86-88°C.
[0024] Virahol enters the upper part of the reaction section 2 of the pressurized reactive distillation column C1 through the feed pipe S01 at a rate of 300.5kg / h, and methyl acetate reclaims with methyl acetate at a rate of 370.4kg / h through S02 The 359.6kg / h circulating material extracted from the circulation pipe S10 at the top of the tower C2 is mixed and then enters the lower part of the reaction section 2 of the pressurized reaction distillation column C1, and ...
Embodiment 2
[0028] Attached figure 1 In the process flow shown, the pressurized reactive distillation column C1 has a diameter of 800 mm, 25 meters of structured packing inside, and 60 theoretical plates; among them, there are 12 plates in the rectification section, 41 plates in the reaction section, and 7 plates in the stripping section. The operating pressure is 2.5 atm, the operating reflux ratio is 1.9, the temperature at the bottom of the tower is 118-121°C, and the temperature at the top of the tower is 81-83°C.
[0029] Virahol enters the upper part of the reaction section 2 of the pressurized reactive distillation column C1 through the feed pipe S01 at a rate of 300.5kg / h, and methyl acetate comes from the normal through the feed pipe S02 and through S10 at a rate of 370.4kg / h. The 449.5kg / h circulating material at the top of the pressurized methyl acetate recovery tower C2 is mixed and then enters the lower part of the reaction section 2 of the pressurized reaction distillation c...
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