A kind of method and device for preparing diphenyl carbonate by one-step method of phenol and dimethyl carbonate
A technology of dimethyl carbonate and diphenyl carbonate, which is applied in the field of organic synthesis, can solve problems such as geometric or positional isomerization side reactions, complicated post-treatment, and a large amount of industrial waste water, and achieve low cost, good catalytic effect, and device The effect of simple structure
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Embodiment 1
[0023] Embodiment 1: a kind of device that phenol and dimethyl carbonate one-step method prepares diphenyl carbonate comprises autoclave 1, extraction tower 2, catalyst recovery device 3, rectifying tower 4, condenser 5, reflux tank 6, The first drying tower 7, the second drying tower 8, the product tank 9, the high pressure reactor 1 is equipped with a PTFE inner cylinder, and the external connection temperature indicator 10 and pressure regulator 11, constantly adjust the pressure during the reaction process, improve the carbonic acid The productive rate of diphenyl ester, dimethyl carbonate raw material tank outlet is connected with described autoclave 1 inlet a, and phenol, ionic liquid catalyst raw material tank outlet is connected with described autoclave 1 inlet b, and described autoclave 1 The outlet is connected to the inlet of the extraction tower 2, the outlet of the inorganic phase of the extraction tower is connected to the inlet of the catalyst recovery device 3, ...
Embodiment 2
[0028] Embodiment 2: Dimethyl carbonate and phenol are dropped into the reactor at a feed ratio of 3: 1, and 0.8wt% of [(C 2 h 5 ) 3 N(CH 2 ) 4 SO 3 H][HSO 4 ] ionic liquid catalyst, heat up and reflux reaction under stirring conditions, the reaction temperature is 160 ° C, the reaction time is 2h, after the reaction is completed, the organic phase mixture is obtained by static separation, and the organic phase mixture is decompressed and refined under a vacuum degree of 5mmHg. Distilled and collected to obtain diphenyl carbonate product.
[0029] The device used in this embodiment is the same as in Example 1, the conversion rate of phenol is 92.5%, and the single pass yield of diphenyl carbonate is 31.2%.
Embodiment 3
[0030] Embodiment 3: dimethyl carbonate and phenol are dropped into reactor according to feed ratio 6: 1, and add 3wt% [(CH 3 ) 3 N(CH 2 ) 4 SO 3 H][HSO 4 ] ionic liquid catalyst, heat up and reflux reaction under stirring conditions, the reaction temperature is 180 ° C, the reaction time is 5h, after the reaction is completed, the organic phase mixture is obtained by standing still for liquid separation, and the organic phase mixture is decompressed and refined under a vacuum degree of 7mmHg. Distilled and collected to obtain diphenyl carbonate product.
[0031] The device used in this embodiment is the same as in Example 1, the conversion rate of phenol is 92.8%, and the single pass yield of diphenyl carbonate is 30.1%.
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