摘要:
Provided is a method for producing diphenyl carbonate, comprising a first purification step of continuously introducing a reaction mixture containing diphenyl carbonate obtained by specific steps to a high-boiling substance separation column A, and continuously separating by distillation the mixture into a column top component (AT) containing diphenyl carbonate and a column bottom component (AB) containing a catalyst; a specific second purification step; and two specific circulation steps, wherein a mass concentration ratio (DPC/HB) of diphenyl carbonate to a high-boiling substance in the column bottom component (AB) of the high-boiling substance separation column A is 0.1 to 1.0, and a mass concentration ratio (DPC/catalyst) of the diphenyl carbonate to the catalyst is 1.0 to 10.0.
摘要:
Provided is a method for industrially producing high-purity diaryl carbonate, comprising: a first purification step of continuously introducing a mixture containing diaryl carbonate to a purifying column A having a side cut discharge port, and continuously separating by distillation the mixture into a column top component (At), a side cut component (As) containing diaryl carbonate, and a column bottom component (Ab) containing a catalyst; and a second purification step of continuously introducing the side cut component (As) to a diaryl carbonate purifying column B having a side cut discharge port, and continuously separating by distillation the component into three components, a column top component (Bt), a side cut component (Bs), and a column bottom component (Bb), thereby obtaining high-purity diaryl carbonate as the side cut component (Bs).
摘要:
A process for producing a high-purity dimethyl carbonate, which includes: (I) cooling a commercial grade dimethyl carbonate containing 1 ppm or more of chlorine to a temperature from +6° C. to −5° C. at a rate from 0.5-2° C./hour, to obtain a first solid dimethyl carbonate; (II) heating the first solid dimethyl carbonate to a temperature from −5° C. to +6° C. at a rate of 1-5° C./hour, to obtain a mixture comprising a second solid dimethyl carbonate and a predetermined amount of a first liquid dimethyl carbonate; (III) separating the first liquid dimethyl carbonate from the mixture, to obtain the second solid dimethyl carbonate; (IV) heating the second solid dimethyl carbonate to a temperature from 20° C. to 40° C., to obtain a second liquid dimethyl carbonate, wherein the second liquid dimethyl carbonate has a purity degree higher than 99.99% and a chlorine content lower than or equal to 1 ppm.
摘要:
Verfahren zur Reinigung von Diarylcarbonaten in wenigstens einer Destillationskolonne enthaltend wenigstens einen Verstärkungsteil im oberen Teil der Kolonne und wenigstens einen Abtriebsteil im unteren Teil der Kolonne, dadurch gekennzeichnet, dass . das zu reinigende Diarylcarbonat durch Umesterung aus wenigstens einem Dialkylcarbonat und wenigstens einer aromatischen Hydroxyverbindung in Gegenwart wenigstens eines Umesterungskatalysator hergestellt wurde und Katalysator aus der Herstellung des Diarylcarbonats als Verunreinigung enthält, . das gereinigte Diarylcarbonat im Seitenstrom der ersten Destillationkolonne entnommen wird.
摘要:
The invention aims at providing a specific process for mass production of dialkyl carbonate and diol by a reaction -distillation process of feeding a raw material consisting of a cyclic carbonate and an aliphatic monohydric alcohol continuously into a continuous multi-stage distillation column to conduct reaction and distillation simultaneously in the column, which enables long-time stable production of both with high selectivity and high productivity and long-time stable and efficient separation and purification of product dialkyl carbonate. It has been found that the production of dialkyl carbonate and diol with respective high selectivities of 95% or above and stable production of high-purity dialkyl carbonate on an industrial scale of at least two tons per hour over a long term of 1000 hours or longer in a high yield are attained by conducting the reaction and distillation in a continuous multi-stage distillation column (A) having a specific structure and separating the obtained overhead component (AT) through distillation by the use of a continuous multi-stage distillation column (B) having a specific structure.