Method for purifying diacid dimethyl esters by plate distillation separation
A technology for dimethyl dibasic acid and dimethyl succinate, which is applied in the field of separation and purification of organic mixtures, can solve the problems of large equipment investment, high production cost, complicated production process and production process, and achieves simplified process flow and reduced production cost. Stable and uniform effect of energy consumption and product quality
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Embodiment 1
[0021] The raw material dimethyl mixed diacid passes through three distillation towers connected in series in sequence, and first enters the first distillation tower connected in series. The pressure inside the first distillation tower is 20kPa, the gas phase temperature at the top of the tower is 95°C, and the temperature at the bottom of the tower is 115°C. ℃, the light component is separated from the top of the first distillation tower, and the bottom material enters the second distillation tower. The bottom of the second distillation tower is vertically equipped with a partition to divide the lower cavity of the second distillation tower into The first tower chamber on one side and the second tower chamber on the other side, and the material inlet of the second distillation tower is located below the top of the partition, the pressure inside the second distillation tower is 18kPa, and the gas phase temperature at the top of the tower is 100°C , the temperature at the bottom...
Embodiment 2
[0023] Dimethyl mixed diacid as the raw material passes through three distillation towers connected in series, and first enters the first distillation tower connected in series. The internal pressure of the first distillation tower is 22kPa, the gas phase temperature at the top of the tower is 100°C, and the temperature at the bottom of the tower is 120°C. ℃, the light component is separated from the top of the first distillation tower, and the bottom material enters the second distillation tower. The bottom of the second distillation tower is vertically equipped with a partition to divide the lower cavity of the second distillation tower into The first tower chamber on one side and the second tower chamber on the other side, and the material inlet of the second distillation tower is located below the top of the partition, the pressure inside the second distillation tower is 19kPa, and the gas phase temperature at the top of the tower is 105°C , the temperature at the bottom of...
Embodiment 3
[0025] The raw material mixed diacid dimethyl ester passes through three distillation towers connected in series in turn, and first enters the first distillation tower connected in series. The pressure inside the first distillation tower is 23kPa, the gas phase temperature at the top of the tower is 105°C, and the temperature at the bottom of the tower is 130°C. ℃, the light component is separated from the top of the first distillation tower, and the bottom material enters the second distillation tower. The bottom of the second distillation tower is vertically equipped with a partition to divide the lower cavity of the second distillation tower into The first tower chamber on one side and the second tower chamber on the other side, and the material inlet of the second distillation tower is located below the top of the partition, the pressure inside the second distillation tower is 20kPa, and the gas phase temperature at the top of the tower is 110°C , the temperature at the bot...
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