Method for intermittent preparing diisopropyl ester amber acid
A technology of diisopropyl succinate and succinic acid, which is applied in the field of preparation of diisopropyl succinate, can solve the problems of many equipment, large material and energy consumption, large investment, etc. The effect of relatively low material consumption and low energy consumption
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[0031] (1) 140 kilograms of succinic acid, 250 kilograms of isopropanol, 2.1 kilograms of 98% sulfuric acid and 70 kilograms of toluene are added into an esterification reactor with a fractionation tower top provided with a condenser and a water separator, heated to the reaction The temperature of the kettle is 83°C, and the vapor phase temperature of the condenser is 76.5±0.5°C. Under reflux, the esterification reaction is carried out until the water separator is free of water, and the temperature of the reactor is gradually increased to 98°C, and the vapor phase temperature of the condenser is greater than 77°C, reclaim the dehydrating agent and excess isopropanol in the reactor, then carry out post-treatment and refining of the crude ester generated by the esterification reaction, and collect 52 kg of the previous fraction;
[0032] (2) the dehydrating agent that 100 kilograms of steps (1) reclaims and excessive Virahol and 140 kilograms of succinic acid, 150 kilograms of Vi...
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