Device and method used for producing ethylene glycol diacetate from low concentration glycol
A technology of diacetate and ethylene glycol, which is applied in the field of production of ethylene glycol diacetate, can solve the problems of ethylene glycol waste, economic benefit reduction, environmental protection pressure, and inability to produce benefits, etc., to achieve excellent product quality , Obvious economic benefits and environmental advantages
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Embodiment 1
[0066] A method utilizing low-concentration ethylene glycol to produce high-concentration ethylene glycol diacetate, specifically comprising the following steps:
[0067] (1) Esterification reaction: Acetic acid and ethylene glycol (molar ratio is 2.4:1) are heated to 65-70°C by the preheater, and then passed into the fixed bed reactor through the feed port I, and the space velocity is 0.8h -1 , acetic acid and ethylene glycol are catalyzed by catalyst A in the fixed-bed reactor to carry out esterification reaction under the conditions of 65-70°C and 0.7-0.8Mpa to obtain the primary reaction product; the primary reaction product flows through the discharge Port I and feed port II enter the catalytic distillation tower;
[0068] The ethylene glycol raw material is the waste produced in the ethylene glycol production process, wherein the concentration of ethylene glycol is 30%, the concentration of heavy substances that do not participate in the reaction is 10%, and the rest is...
Embodiment 2
[0085] A method utilizing low-concentration ethylene glycol to produce high-concentration ethylene glycol diacetate, specifically comprising the following steps:
[0086] (1) Esterification reaction: Acetic acid and ethylene glycol (molar ratio is 2.4:1) are heated to 65-70°C by the preheater, and then passed into the fixed bed reactor through the feed port I, and the space velocity is 0.8h -1 , acetic acid and ethylene glycol are catalyzed by catalyst A in the fixed-bed reactor to carry out esterification reaction under the conditions of 65-70 ° C and 0.7-0.8 MPa to obtain primary reaction products; the primary reaction products flow through the discharge Port I and feed port II enter the catalytic distillation tower;
[0087] The ethylene glycol raw material is the waste produced in the ethylene glycol production process, wherein the concentration of ethylene glycol is 50%, the concentration of heavy substances that do not participate in the reaction is 10%, and the rest is...
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