Purification method for polyformaldehyde dimethyl ether
A technology of dimethyl ether and purification method, which is applied in chemical instruments and methods, preparation of organic compounds, organic chemistry, etc., can solve the problem of unfavorable expansion of production, affecting the continuous and stable operation of polyoxymethylene dimethyl ether separation process, and processing time long wait question
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Embodiment 1
[0037] The reaction equilibrium mixture obtained by catalytic reaction of paraformaldehyde and methylal as raw materials is firstly rectified by the first rectification tower at atmospheric pressure to remove the first fraction to obtain the first tower still liquid with a temperature of 105°C. The first tower still liquid enters the lower section of the purification tower from the bottom through the insulation pipeline, and the lower section of the purification tower is filled with Ca(OH) 2 As the filler, the upper section is filled with anhydrous calcium chloride, the temperature of the purification tower is 100°C, the residence time of the lower section is 10min, and the top of the tower contains methanol and PODE 2-5 Purification tower material. The output from the purification tower enters the methanol removal tower, where the operating pressure is normal pressure, the reflux ratio is 0.3, and the temperature of the bottom of the tower is 110°C, and the distillate contain...
Embodiment 2
[0041] The reaction equilibrium mixture obtained by catalytic reaction of paraformaldehyde and methylal as raw materials is firstly rectified by the first rectification tower at atmospheric pressure to remove the first fraction to obtain the first tower still liquid with a temperature of 105°C. The first tower kettle liquid enters the lower part of the purification tower from the bottom through the insulation pipeline. The lower part of the purification tower uses NaOH as the filler, and the upper part uses anhydrous calcium chloride as the filler. Contains methanol and PODE 2-5 Purification tower material. The output from the purification tower enters the methanol removal tower, where the operating pressure is normal pressure, the reflux ratio is 0.3, and the temperature of the bottom of the tower is 110°C, and the distillate containing methanol is extracted from the top of the tower. The bottom liquid of the methanol removal tower enters the second rectification tower and t...
Embodiment 3
[0043] The reaction equilibrium mixture obtained by catalytic reaction of paraformaldehyde and methylal as raw materials is firstly rectified by the first rectification tower at atmospheric pressure to remove the first fraction to obtain the first tower still liquid with a temperature of 105°C. The first tower still liquid enters the lower section of the purification tower from the bottom through the insulation pipeline, and the lower section of the purification tower is filled with Ca(OH) with a weight ratio of 1:1 2 The mixture with NaOH is used as filler, the upper section is filled with anhydrous calcium chloride, the temperature of the purification tower is 100°C, the residence time of the lower section is 10min, and the top of the tower contains methanol and PODE 2-5 Purification tower material. The output from the purification tower enters the methanol removal tower, where the operating pressure is normal pressure, the reflux ratio is 0.3, and the temperature of the bot...
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