A kind of production method of safe and environment-friendly carbonate-based mixed solvent
A mixed solvent, safe and environmentally friendly technology, applied in the chemical industry, can solve the problems of catalyst deactivation of strong alkaline catalysts and carbonate catalysts, high price of carbonate solvents, non-existence, etc., to achieve difficult deactivation, high activity, low cost effect
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Embodiment 1
[0020] The transesterification reaction is carried out under normal pressure in the reactor, and the raw materials are dimethyl carbonate, ethanol and ethyl acetate; the catalyst is sodium methoxide and dibutyltin oxide; the mole of dimethyl carbonate, ethanol and ethyl acetate The ratio is 1:0.75:0.25; the amount of catalyst sodium methylate and dibutyltin oxide is respectively 0.75wt% and 0.25wt% of the total amount of raw materials (dimethyl carbonate, ethanol and ethyl acetate). The transesterification reaction is divided into two stages, the reaction temperature of the first stage is 80° C., and the reaction time is 20 minutes; the reaction temperature of the second stage is 120° C., and the reaction time is 30 minutes. After separation of low-boiling substances with a boiling point of methanol below 70°C by distillation, the obtained fraction content of 90-91°C is: 15.8wt%, and the fraction content of 108-110°C is: 21.5wt%, and the fraction content of 126-128°C For: 18.5...
Embodiment 2
[0022] Carry out transesterification reaction under the pressure condition of 0.2MPa in the reactor, the molar ratio of raw material dimethyl carbonate and ethanol, isobutyl acetate is 1: 1: 0.5; 1.0 wt% and 0.50 wt% of the total amount. The transesterification reaction is divided into two stages, the reaction temperature of the first stage is 80°C, and the reaction time is 20min; the reaction temperature of the second stage is 130°C, and the reaction time is 30min. After separation of low-boiling substances with a boiling point of methanol below 70°C by distillation, the obtained fraction content of 90-91°C is: 10.2wt%, and the fraction content of 108-110°C is: 18.5wt%, and the fraction content of 126-128°C For: 25.5wt%, fraction above 130°C: 15.7wt%. The carbonate-based mixed solvent obtained in the present invention can replace paint solvents containing 90-140°C boiling point components, such as toluene, xylene series, etc.; and the toxicity of the carbonate-based mixed so...
Embodiment 3
[0024] The transesterification reaction is carried out under the pressure condition of 0.2MPa in the reactor, the molar ratio of the raw material dimethyl carbonate, isopropanol and isobutyl acetate is 1:1:0.5; the catalyst is sodium ethylate, triethanolamine and tetratitanate The consumption of butyl ester is respectively 0.5wt%, 0.5wt% and 0.5wt% of the total amount of raw materials. The transesterification reaction is divided into two stages. The reaction temperature of the first stage is 85° C., and the reaction time is 20 minutes; the reaction temperature of the second stage is 135° C., and the reaction time is 30 minutes. After separation of low-boiling substances with a boiling point of methanol below 70°C by distillation, the obtained fraction content of 90-91°C is: 10.5wt%, and the fraction content of 108-110°C is: 17.5wt%, and the fraction content of 126-128°C For: 28.5wt%, fraction above 130°C: 20.1wt%. The carbonate-based mixed solvent obtained in the present inve...
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