A continuous rectification system for producing alcohol ester twelve and its method for producing alcohol ester twelve
A technology of 12. rectification of alcohol esters, applied in separation methods, chemical instruments and methods, separation/purification of carboxylic acid esters, etc. The effect of improved efficiency, improved production efficiency, and shorter reaction time
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Embodiment 1
[0028] Utilize the method for the system production alcohol ester twelve of above-mentioned continuous rectification to produce alcohol ester twelve, comprise the steps:
[0029] (1) The raw material of isobutyraldehyde (industrial grade) enters from the upper part of the third packing section of the reactive distillation column 1 through the first metering pump 61 at a feed rate of 2 tons / hour; the catalyst solution passes through the second metering pump 62 Enter the feed port of the lower part of the third packing section of the reactive distillation column 1 with a feed rate of 80kg / hour (that is, the amount of catalyst added is 2% of the mass of isobutyraldehyde);
[0030] (2) When the liquid level of the reaction distillation tower 1 reaches 50%, the reaction distillation tower 1 is heated by opening the tower heating reboiler and the condensed water at the top of the tower, so that the temperature of the reaction distillation tower 1 tower rises to 72°C, when the liquid...
Embodiment 2
[0035] Utilize the method for the system production alcohol ester twelve of above-mentioned continuous rectification to produce alcohol ester twelve, comprise the steps:
[0036] (1) The raw material of isobutyraldehyde (industrial grade) enters from the upper part of the third packing section of the reactive distillation column 1 through the first metering pump 61 at a feed rate of 3.5 tons / hour; the catalyst solution passes through the second metering pump 62 Enter the feed port of the lower part of the third packing section of the reactive distillation column 1 with a feed rate of 210kg / hour (that is, the amount of catalyst added is 3% of the mass of isobutyraldehyde);
[0037] (2) When the liquid level of the reaction distillation tower 1 reaches 50%, the reaction distillation tower 1 is heated by opening the tower heating reboiler and the condensed water at the top of the tower, so that the temperature of the reaction distillation tower 1 tower rises to 72°C, when the liq...
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