Method for separating sec-butyl acetate from reaction mixture of acetic acid and hybrid C4
A kind of sec-butyl acetate and the technology after the reaction are applied in the field of separating sec-butyl acetate, and can solve the problems such as it is difficult to fully separate sec-butyl acetate and acetic acid.
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Embodiment 1
[0027] Embodiment 1: The mass composition is the mixture of 45.03% of sec-butyl acetate, 37.29% of acetic acid, 17.68% of hydrocarbons and other substances into the flash tower. The temperature at the bottom of the flash tower is 180.5°C, the temperature at the top of the flash tower is 56°C, and the pressure is 0.65MPa. The mass composition of the flash distillation bottom product obtained is: 52.21% of sec-butyl acetate, 43.24% of acetic acid, 4.55% of hydrocarbons and other substances.
[0028] The bottom material of the flashing tower enters the azeotropic rectification tower, and the entrainer water is added into the azeotropic rectification tower in the ratio of sec-butyl acetate: water=4:1 (mass percentage) simultaneously. The temperature at the bottom of the azeotropic distillation column is 125°C, and the temperature at the top of the column is 87.5°C. The mass composition of the overhead distillate obtained is: 94.07% of sec-butyl acetate, 0.1% of acetic acid, 4.83%...
Embodiment 2
[0031] Embodiment 2: The mass composition is the mixture of 51.38% of sec-butyl acetate, 36.10% of acetic acid, 12.52% of hydrocarbons and other substances into the flash tower. The temperature at the bottom of the flash tower is 165°C, the temperature at the top of the flash tower is 77°C, and the pressure is 0.48 MPa. The mass composition of the flash distillation bottom product obtained is: 55.98% of sec-butyl acetate, 40.29% of acetic acid, 3.73% of hydrocarbons and other substances.
[0032] The bottom material of the flashing tower enters the azeotropic rectification tower, and the entrainer water is added into the azeotropic rectification tower in the ratio of sec-butyl acetate: water=4:1 (mass percentage) simultaneously. The temperature at the bottom of the azeotropic distillation column is 115°C, and the temperature at the top of the column is 82.5°C. The mass composition of the overhead distillate obtained is: 95.13% of sec-butyl acetate, 0.04% of acetic acid, 3.83%...
Embodiment 3
[0035] Embodiment 3: The mass composition is the mixture of 44.98% of sec-butyl acetate, 36.53% of acetic acid, 18.49% of hydrocarbons and other substances into the flash tower. The temperature at the bottom of the flash tower is 188°C, the temperature at the top of the flash tower is 57°C, and the pressure is 0.56 MPa. The mass composition of the bottom product obtained from the flash distillation tower is: 52.49% of sec-butyl acetate, 42.78% of acetic acid, 4.73% of hydrocarbons and other substances.
[0036] The bottom material of the flashing tower enters the azeotropic rectification tower, and the entrainer water is added into the azeotropic rectification tower in the ratio of sec-butyl acetate: water=4:1 (mass percentage) simultaneously. The temperature at the bottom of the azeotropic distillation column is 121°C, and the temperature at the top of the column is 86.5°C. The mass composition of the overhead distillate obtained is: 94.84% of sec-butyl acetate, 0.07% of ace...
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