Method for preparing methyl p-tert-butylbenzoate
A technology for methyl tert-butyl benzoate and tert-butyl benzoic acid, applied in the field of preparing methyl tert-butyl benzoate, can solve the problems of large environmental pollution, easy water loss of organic matter, easy hydrolysis of catalysts, etc. Environmentally friendly, easy to industrialize, easy to separate
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Embodiment 1
[0032] Add the raw materials of methanol and p-tert-butylbenzoic acid with a molar ratio of 10:1 into the reactor, then add a polystyrene sulfonic acid resin catalyst with a raw material weight percentage of 10%, heat, and at a reaction temperature of 100°C, the reaction pressure Under the condition of 1Mpa, stir to carry out the esterification reaction. After reacting for 8 hours, the reaction solution was discharged and centrifuged, and the obtained upper product was the crude product of methyl p-tert-butylbenzoate, water and a small amount of raw materials p-tert-butylbenzoic acid and methanol, and the upper product was rotary-evaporated to remove methanol , water, and then rotary steaming to obtain the target product methyl p-tert-butylbenzoate, wherein unreacted p-tert-butylbenzoic acid and methanol are recycled, and the lower layer catalyst is recycled. The yield of methyl p-tert-butylbenzoate is 95%, and the purity is more than or equal to 99.99%.
Embodiment 2
[0034] Add the raw materials of methanol and p-tert-butylbenzoic acid with a molar ratio of 10:1 into the reactor, and then add a perfluorosulfonic acid resin catalyst with a raw material weight percentage of 10%, and heat it at a reaction temperature of 120°C and a reaction pressure of 1.5 Under the condition of Mpa, stir, carry out esterification reaction. After reacting for 5 hours, the reaction solution was discharged and centrifuged, and the obtained upper product was the crude product of methyl p-tert-butylbenzoate, water and a small amount of raw materials p-tert-butylbenzoic acid and methanol, and the upper product was rotary-evaporated to remove methanol , water, and then rotary steaming to obtain the target product methyl p-tert-butylbenzoate, wherein unreacted p-tert-butylbenzoic acid and methanol are recycled, and the lower layer catalyst is recycled. The yield of methyl p-tert-butylbenzoate is 96%, and the purity is more than or equal to 99.99%.
Embodiment 3
[0036] Add the raw materials of methanol and p-tert-butylbenzoic acid with a molar ratio of 10:1 into the reactor, then add a polystyrenesulfonic acid resin catalyst with a raw material weight percentage of 15%, heat, and at a reaction temperature of 120°C, a reaction pressure of Under the condition of 1.5Mpa, stir to carry out esterification reaction. After reacting for 3 hours, the reaction liquid was discharged and centrifuged, and the obtained upper product was the crude product of methyl p-tert-butylbenzoate, water and a small amount of raw materials p-tert-butylbenzoic acid and methanol, and the upper product was rotary-evaporated to remove methanol , water, and then rotary steaming to obtain the target product methyl p-tert-butylbenzoate, wherein unreacted p-tert-butylbenzoic acid and methanol are recycled, and the lower layer catalyst is recycled. The yield of methyl p-tert-butylbenzoate is 94%, and the purity is more than or equal to 99.99%.
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