Method for continuously synthesizing diphenyl carbonate by micro reactor
A technology of diphenyl carbonate and microreactor, which is applied in the preparation of organic carbonate, organic chemistry, etc., can solve the problems of low selectivity and yield, and achieve the advantages of simple process flow, good heat transfer efficiency and saving production cost. Effect
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Embodiment 1
[0028] Experiments were carried out according to this method, and microreactors were designed by themselves. One feed port of the microreactor is equipped with a dispersing membrane, and the dispersing membrane is a 500-mesh membrane. The cross-sectional area of the reaction channel of the microreactor is 0.05×0.05 (mm 2 ), the runner length is 30cm.
[0029] Add 376g of phenol and 15.7g of homogeneous catalyst into the mixing tank, heat, stir, and mix evenly, then add 609g of methyl phenyl carbonate, continue to stir, mix evenly, the molar ratio of phenol and methyl phenyl carbonate The molar ratio of phenol and homogeneous catalyst is 1:1, and the molar ratio of phenol and homogeneous catalyst is 1:0.01; the feed liquid is transported to the microreactor with two advection pumps, the flow rate is 1ml / min respectively, and a stream of material at the feed inlet passes through the dispersion membrane The sheet is sprayed onto another stream of material to carry out the syn...
Embodiment 2
[0031] Experiments were carried out according to this method, and microreactors were designed by themselves. One feed port of the microreactor is equipped with a dispersing membrane, and the dispersing membrane is a 2000-mesh membrane. The cross-sectional area of the reaction channel of the microreactor is 0.4×0.4 (mm 2 ), the runner length is 1m.
[0032] Add 376g of phenol and 31.4g of homogeneous catalyst into the mixing tank, heat, stir, and mix well, then add 1218g of methyl phenyl carbonate, continue to stir, mix well, the molar ratio of phenol and methyl phenyl carbonate The molar ratio of phenol to homogeneous catalyst is 1:0.02; two advection pumps are used to transport the feed liquid to the microreactor, the flow rate is 0.5mL / min respectively, and a stream of material at the feed inlet passes through the dispersed The diaphragm is sprayed onto another stream of material to carry out the synthesis reaction. The temperature of the reaction system is 200°C. Adjust...
Embodiment 3
[0034] Experiments were carried out according to this method, and microreactors were designed by themselves. One feed port of the microreactor is equipped with a dispersing membrane, and the dispersing membrane is a 1500-mesh membrane. The cross-sectional area of the reaction channel of the microreactor is 0.25×0.25 (mm 2 ), the runner length is 2m.
[0035] Add 376g of phenol and 31.4g of homogeneous catalyst into the mixing tank, heat, stir, and mix well, then add 1218g of methyl phenyl carbonate, continue to stir, mix well, the molar ratio of phenol and methyl phenyl carbonate The molar ratio of phenol and homogeneous catalyst is 1:02; two advection pumps are used to transport the feed liquid to the microreactor, the flow rate is 1ml / min respectively, and a stream of material at the feed inlet passes through the dispersion membrane The sheet is sprayed onto another stream of material to carry out the synthesis reaction. The temperature of the reaction system is 220°C. A...
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