A method for purifying 2,2-dimethoxyacetaldehyde
A technology of dimethoxyacetaldehyde and reaction liquid, which is applied in the field of separation and purification of fine chemicals, can solve the problems not clearly mentioned, high energy consumption, large reflux ratio, etc., to reduce energy consumption, improve production efficiency, The effect of reducing the reflux ratio
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Embodiment 1
[0014] 2000g of the 2,2-dimethoxyacetaldehyde reaction solution prepared by reacting glyoxal with methanol was subjected to ordinary atmospheric distillation, and the 2,2-dimethoxyacetaldehyde reaction solution was heated to 85°C until no longer End when there is a distillate, the remaining solution 800g is used as rectification raw material, the mass percent composition of 2,2-dimethoxyacetaldehyde detected by gas chromatography is 60%, the mass percentage of 2,2-dimethoxyacetaldehyde 480g, add 600g of extractant water, mix evenly, add to the tower still of the rectifying tower, the theoretical plate number of the rectifying tower is 30, be that 90Kpa in absolute vacuum, the reaction liquid temperature of tower still begins to refine Distillation, control the reflux ratio to 0.6:1, collect the fraction before 40-50°C, continue heating to 80°C, control the reflux ratio to 10:1, collect the fraction at 50-60°C to obtain 2,2-dimethoxyacetaldehyde 326g, the gas chromatography det...
Embodiment 2
[0016] 2000g of the 2,2-dimethoxyacetaldehyde reaction solution obtained by reacting glyoxal with methanol was subjected to normal pressure distillation, and the 2,2-dimethoxyacetaldehyde reaction solution was heated to 90°C until no longer End when a fraction is distilled off, the remaining solution 720g is used as rectification raw material, the mass percent composition of 2,2-dimethoxyacetaldehyde detected by gas chromatography is 65%, the mass percentage of 2,2-dimethoxyacetaldehyde is 468g, add extractant water 600g, mix uniformly, add the tower still of rectifying tower, the theoretical plate number of rectifying tower is 30, be that 90Kpa, tower still reaction liquid temperature start refining under the condition of 60 ℃ in absolute vacuum degree Distillation, control the reflux ratio to 0.6:1, collect the fraction before 40-50°C, continue heating to 80°C, control the reflux ratio to 10:1, collect the fraction at 50-60°C to obtain 2,2-dimethoxyacetaldehyde 323g, the pur...
Embodiment 3
[0018] 2000g of the 2,2-dimethoxyacetaldehyde reaction solution prepared by reacting glyoxal with methanol was subjected to ordinary atmospheric distillation, and the 2,2-dimethoxyacetaldehyde reaction solution was heated to 85°C until no longer End when there is a distillate, the remaining solution 800g is used as rectification raw material, the mass percent composition of 2,2-dimethoxyacetaldehyde detected by gas chromatography is 60%, the mass percentage of 2,2-dimethoxyacetaldehyde is 480g, add 720g of extractant water, mix well, add the tower still of rectifying tower, the theoretical plate number of rectifying tower is 30, be that 90Kpa, tower still reaction liquid temperature start refining under the condition of 60 ℃ in absolute vacuum degree Distillation, control the reflux ratio to 0.6:1, collect the fraction before 40-50°C, continue heating to 80°C, control the reflux ratio to 10:1, collect the fraction at 50-60°C to obtain 2,2-dimethoxyacetaldehyde 335g, the gas ch...
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