Method and device for preparing tert-butyl acetate
A technology of tert-butyl acetate and acetic acid, which is applied in the field of preparing tert-butyl acetate, can solve the problems of low recovery rate of tert-butyl acetate, low recovery rate of tert-butyl acetate, low recovery rate of tert-butanol, etc., and achieve the purpose of suppressing side effects reaction, increase selectivity and yield, and suppress pyrolysis effects
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Embodiment 1
[0049] Acetic acid and isobutylene are sent into the esterification reactor, and the polymerization inhibitor tert-butanol is added to react under the esterification reaction conditions. The esterification reactor is divided into two sections to control the reaction temperature respectively, and the temperature of the first section of the reaction is controlled to be 18°C, the temperature of the second stage reactor is controlled to be 18°C, the reaction pressure is 0.6MPa, the acid-ene ratio is 3:1, the reaction residence time is 80min, and the addition amount of polymerization inhibitor tert-butanol is 10wt% of the amount of acetic acid addition . The content of the mixture obtained after the reaction is: tert-butyl acetate 20.45wt%, tert-butanol 5.12wt%, acetic acid 68.54wt%, C8 2.12wt%, isobutylene 2.55wt%, water 1.22wt%. Enter the light component removal tower for separation. The top pressure of the light component removal tower is normal pressure, the top temperature is ...
Embodiment 2
[0052] Acetic acid and isobutylene are sent into the esterification reactor, and the polymerization inhibitor tert-butanol is added to react under the esterification reaction conditions. The esterification reactor is divided into two sections to control the reaction temperature respectively, and the temperature of the first section of the reaction is controlled to be 19°C, the temperature of the second stage reactor is controlled to be 20°C, the reaction pressure is 0.7MPa, the acid-to-ene ratio is 4:1, the reaction residence time is 70min, and the amount of polymerization inhibitor tert-butanol added is 8wt% of the amount of acetic acid added . The content of the mixture obtained after the reaction is: tert-butyl acetate 22.12wt%, tert-butanol 3.56wt%, acetic acid 64.77wt%, C8 2.89wt%, isobutylene 5.45wt%, water 1.21wt%. Enter the light component removal tower for separation. The top pressure of the light component removal tower is normal pressure, the top temperature is -8°C...
Embodiment 3
[0055]Acetic acid and isobutylene are sent into the esterification reactor, and the polymerization inhibitor tert-butanol is added to react under the esterification reaction conditions. The esterification reactor is divided into two sections to control the reaction temperature respectively, and the temperature of the first section of the reaction is controlled to be 20°C, control the temperature of the second stage reactor to be 22°C, the reaction pressure is 0.8MPa, the acid-ene ratio is 5:1, the reaction residence time is 60min, and the addition amount of polymerization inhibitor tert-butanol is 6wt% of the amount of acetic acid addition . The content of the mixture obtained after the reaction is: tert-butyl acetate 24.14wt%, tert-butanol 6.45wt%, acetic acid 65.21wt%, C8 1.81wt%, isobutylene 1.22wt%, water 1.17wt%, the mixture after the reaction was sent to Enter the light component removal tower for separation. The top pressure of the light component removal tower is norma...
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