Preparation method of ethylene glycol monoether
A technology of ethylene glycol monoether and aliphatic alcohol, applied in ether preparation, alkylene oxide preparation of ether, organic chemistry, etc., can solve problems such as affecting the economics of the device, the inability of the device to operate stably for a long time, and potential safety hazards.
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Embodiment 1
[0075] With n-butanol as the low carbon aliphatic alcohol participating in the reaction, adopt figure 1The shown rectification tower is used as a reactor, and the structural parameters of the rectification tower are as follows: the catalytic rectification tower is provided with 17 theoretical plates, the feed ports of n-butanol and triethylamine are all arranged on the second plate, and the ethylene oxide The feeding port 5 is arranged on the twelfth plate.
[0076] The operating conditions of the catalytic rectification tower: the operating pressure is 0.2MPa, the feed flow rate of ethylene oxide is 2.27kmol / h, the feed molar flow ratio of n-butanol and ethylene oxide is 1.3:1, triethylamine and oxide The feed molar flow ratio of ethane is 0.04:1, the liquid holdup is 70L, and the reboil ratio is 9.
[0077] During the reaction process, the non-condensable gas is discharged through the second condenser 23, and there is no extraction at the top of the tower, and the liquid ph...
Embodiment 2
[0081] Take ethanol as the low-carbon aliphatic alcohol participating in the reaction, and adopt the rectifying tower identical with embodiment 1 to carry out reaction.
[0082] Among them, the operating conditions of the catalytic rectification tower: the operating pressure is 0.3MPa, the ethylene oxide feed flow rate is 2.27kmol / h, the feed molar flow ratio of ethanol and ethylene oxide is 1.1:1, triethylamine and cyclic The feed molar flow ratio of oxyethane is 0.04:1, the liquid holdup is 70L, and the reboil ratio is 8.
[0083] During the reaction process, the non-condensable gas is discharged through the second condenser 23, and there is no extraction at the top of the tower, and the liquid phase product extracted from the tower reactor is cooled and then analyzed by chromatography.
[0084] The molar composition of the tower still product is: ethanol 18.71%, ethylene glycol monoethyl ether 72.80%, diethylene glycol monoethyl ether 5.41%, triethylene glycol monoethyl eth...
Embodiment 3
[0087] Take methanol as the low-carbon aliphatic alcohol participating in the reaction, and adopt the same rectifying tower as in Example 1 to carry out the reaction.
[0088] Among them, the operating conditions of the catalytic rectification tower: the operating pressure is 0.4MPa, the ethylene oxide feed flow rate is 2.27kmol / h, the feed molar flow ratio of n-butanol and ethylene oxide is 1.1:1, triethylamine and The feed molar flow ratio of ethylene oxide is 0.03:1, the liquid holdup is 50L, and the reboil ratio is 10.
[0089] During the reaction process, the non-condensable gas is discharged through the second condenser 23, and there is no extraction at the top of the tower, and the liquid phase product extracted from the tower reactor is cooled and then analyzed by chromatography.
[0090] The molar composition of the bottom product is: methanol 18.78%, ethylene glycol monomethyl ether 72.51%, diethylene glycol monomethyl ether 6.20%, triethylene glycol monomethyl ether...
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