Ethylene glycol diacetate or propylene glycol diacetate production system and method
A technology of propylene glycol diacetate and ethylene glycol diacetate, which is applied in the field of diol diacetate preparation, can solve problems such as difficult product separation, many by-products, complicated process flow, etc., so as to improve product purity and increase  The effect of production efficiency
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Embodiment 1~7
[0022] A production process of ethylene glycol diacetate, according to the formula in parts by weight: 1 part of catalyst, 10-20 parts of ethylene glycol, 20-200 parts of acetic acid, 30-100 parts of water-carrying agent are added to reactor 2, normal pressure, reaction The temperature is 110~150°C, and the reaction is 10~50h; the reacted materials continue to enter the light removal tower 4 from the bottom of the reaction kettle 2, and the light removal tower 4 controls the top temperature of the tower to 110~140°C, and the pressure is normal pressure; the materials obtained from the tower kettle enter Weight removal tower, weight removal tower 5 vacuum degree -0.093~-0.097MPa, control tower top temperature 130~140°C, and get ethylene glycol diacetate at the top of the tower.
[0023] Wherein, filter screen is arranged in reactor 2 to do dividing plate, and the macroporous cation exchange resin catalyst of sulfonic acid treatment is placed above dividing plate; Reactor 2 top c...
Embodiment 8~14
[0029] A kind of propylene glycol diacetate production technology, it is characterized in that: formula according to weight: 1 part of catalyst, 10-20 parts of propylene glycol, 20-200 parts of acetic acid, 30-100 parts of water-carrying agent are added to reactor 2, normal pressure, reaction The temperature is 110~150°C, and the reaction is 10~50h; the reacted material enters the light removal tower 4 from the bottom of the reaction kettle 2, and the light removal tower 4 controls the top temperature of the tower to 110~140°C, and the pressure is normal pressure; the material obtained from the tower kettle enters the light removal tower 4 Heavy tower, weight-removing tower 5 vacuum degree -0.093~-0.097MPa, control tower top temperature 130~140°C, the top of the tower can obtain propylene glycol diacetate, adopt the same production system as in Example 1.
[0030] Wherein, filter screen is arranged in reactor 2 to do dividing plate, and the macroporous cation exchange resin cat...
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