Process for synthesizing dibutyl carbonate
A technology of dibutyl carbonate and dimethyl carbonate, which is applied in the field of catalytic synthesis of dibutyl carbonate with supported catalysts, can solve the problems of low conversion rate of raw materials, production process, environmental pollution, toxicity, etc., and achieve high conversion rate of raw materials, Ease of separation and mild reaction conditions
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Embodiment 1
[0011] The present invention is a process for preparing dibutyl carbonate by using dimethyl carbonate and butanol as raw materials under heterogeneous catalytic reaction conditions. The reaction is carried out in a rotary evaporator, and 0.1mol of industrial grade dimethyl carbonate is used, which is chemically pure. Butanol 0.4mol, supported catalyst KOH / AC2.6g (6% of the raw material quality), wherein the KOH load is 30% of the activated carbon (AC) quality, the oil bath heating temperature is 373K, and the reaction time is 6 hours.
[0012] Since this reaction is a two-step reaction, and both are reversible reactions, the thermodynamic equilibrium constant is very small. In order to break the limitation of thermodynamic equilibrium and improve the conversion rate of raw materials and the selectivity of the target product, 50ml / min of N 2 Pass it into the reaction bottle, take the saturated vapor of methanol out of the reactor, and collect it through a cold trap. After the re...
Embodiment 2
[0014] Industrial grade dimethyl carbonate 0.1mol, chemically pure butanol 0.5mol, supported catalyst KOH / AC2.6g (6% of raw material quality), wherein KOH loading is 10% of activated carbon (AC) quality, oil bath heating The temperature was 363K, the reaction time was 5 hours, other conditions were the same as in Example 1, the conversion rate of dimethyl carbonate was 94.3%, and the selectivity of dibutyl carbonate was 43.26%.
Embodiment 3
[0016] Industrial grade dimethyl carbonate 0.1mol, chemically pure butanol 0.5mol, supported catalyst KOH / AC1.3g (3% of raw material quality), wherein KOH loading is 5% of activated carbon (AC) quality, oil bath heating The temperature was 363K, the reaction time was 5 hours, other conditions were the same as in Example 1, the conversion rate of dimethyl carbonate was 93.88%, and the selectivity of dibutyl carbonate was 38.27%.
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