초록 ▼

A two stage interfacial polycondensation process for the production of carbonic acid diaryl ester is disclosed. The invention concerns an improvement to the process that entails forming in a first stage a reaction mixture that contains an inert solvent, at least one monophenol, phosgene, and aqueous

A two stage interfacial polycondensation process for the production of carbonic acid diaryl ester is disclosed. The invention concerns an improvement to the process that entails forming in a first stage a reaction mixture that contains an inert solvent, at least one monophenol, phosgene, and aqueous alkali hydroxide solution, passing said reaction mixture to a second stage through at least one constriction at a velocity of 3 to 15 m/s under conditions designed to expose the mixture to a pressure drop of 0.1 to 2.5 bar, and in said second stage passing said mixture through at least one dispersing element at a velocity of 2 to 10 m/s under conditions designed to expose the mixture to a pressure drop of 0.1 to 0.5 bar. The resulting product is characterized by its purity and suitability for the manufacture of polycarbonates in the melt transesterification process.

대표청구항 ▼

1. In the interfacial polycondensation process for the production of carbonic acid diaryl ester the improvement comprising forming in a first stage a reaction mixture that contains an inert solvent, at least one monophenol, phosgene, and aqueous alkali hydroxide solution, passing said reaction mixtu

1. In the interfacial polycondensation process for the production of carbonic acid diaryl ester the improvement comprising forming in a first stage a reaction mixture that contains an inert solvent, at least one monophenol, phosgene, and aqueous alkali hydroxide solution, passing said reaction mixture through at least one constriction at a velocity of 3 to 15 m/s under conditions designed to expose the mixture to a pressure drop of 0.1 to 2.5 bar, and in the second stage passing said mixture through at least one dispersing element at a velocity of 2 to 10 m/s under conditions designed to expose the mixture to a pressure drop of 0.1 to 0.5 bar. 2. The process of claim 1 wherein the residence time of the reaction mixture in the first stage is in the range of 2 seconds to 300 seconds. 3. The process of claim 1 wherein the pH of the reaction mixture in the first stage is in the range of 11.0 to 12.0. 4. The process of claim 1 wherein second stage is carried out in a reactor equipped with a plurality of elements to distribute and mix said mixture. 5. The process of claim 4 wherein the residence time per element is less than 0.5 second. 6. The process of claim 5 wherein the residence time between two successive elements is 3 to 12 seconds. 7. The process of claim 1 wherein residence time in the second stage is 1 to 30 minutes.