Method for producing ethyl acetate by using entrainer
A technology of ethyl acetate and entraining agent, which is applied in the field of producing ethyl acetate using entraining agent, which can solve the problems of high energy consumption, large reflux ratio of esterification tower, and limited production capacity of the device, so as to reduce energy consumption and reflux ratio , significant economic effect
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Embodiment 1
[0022] With the raw material that is made up of ethanol, acetic acid (the proportioning of raw material is: the molar percentage composition of ethanol is 48%, the molar percentage composition of acetic acid is 52%), and acetic acid is excessive, guarantees the high acidity of esterification kettle, prevents that ethanol is too much Enter the esterification tower to achieve the purpose of controlling the top composition of the esterification tower as close as possible to the ethyl acetate-water binary azeotropic composition, thereby facilitating the phase separation of the phase separator at the top of the esterification tower and reducing the water content of the crude ester. The entraining agent is added at one time, and the amount of addition is 5% (mass) of the esterification still material, supplemented intermittently in small amounts. use figure 1 The process shown is for esterification reaction-rectification. The reaction temperature of the esterification tank is 104-10...
Embodiment 2
[0028] A raw material composed of ethanol and acetic acid mixture (the ratio of the raw material is: the molar percentage of ethanol is 50%, and the molar percentage of acetic acid is 50%). The entraining agent is added at one time, and the amount of addition is 8% (mass) of the esterification still material, supplemented intermittently in small amounts. use figure 1 The process shown is for esterification reaction-rectification. The reaction temperature of the esterification tank is 105°C and the pressure is 0.125MPa. The temperature of the top of the esterification tower is 71-72°C and the pressure is 0.105MPa. ~90℃, pressure 0.108~0.11MPa, temperature of the stripping tower bottom 80~83℃, pressure 0.108~0.11MPa, stripping tower top temperature 71~72℃, pressure 0.10~0.105MPa.
[0029] The chemical process simulation software ASPEN PLUS was used to simulate and calculate the entire process of the reactor, esterification tower, and stripping tower. The calculation results are...
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