Method and apparatus for purification of dimethyl carbonate using pervaporation
An apparatus for separating dimethyl carbonate using pervaporation includes: an atmospheric distillation column and a high pressure distillation column distilling a mixture containing dimethyl carbonate and methanol and separating dimethyl carbonate from the mixture; and a pervaporation membrane module disposed between the atmospheric distillation column and the high pressure distillation column and allowing for permeation of the methanol to separate the methanol from the mixture, thereby reducing heat consumption and a process cost as compared to the case of only using an existing pressure swing distillation method.
1. An apparatus for purifying dimethyl carbonate using pervaporation, comprising:
an atmospheric distillation column and a high pressure distillation column distilling a mixture containing dimethyl carbonate and methanol and separating dimethyl carbonate from the mixture; and
a pervaporation membrane module disposed between the atmospheric distillation column and the high pressure distillation column and allowing for permeation of the methanol to separate the methanol from the mixture;
wherein the pervaporation membrane module supplies a recovered amount of the mixture to the high pressure distillation column, and wherein on a permeate side, the pervaporation membrane module is operated at a vacuum between 10 to 1,013 mbar,
wherein the atmospheric distillation column supplies an amount of the mixture recovered from an upper portion of the atmospheric distillation column to the pervaporation membrane module,
wherein the pervaporation membrane module supplies a permeation material to the atmospheric distillation column,
wherein the high pressure distillation column supplies an amount of the mixture recovered from an upper portion of the high pressure distillation column to the atmospheric distillation column.
2. The apparatus of claim 1 , wherein the pervaportion membrane module comprises a methanol selective membrane selected from a silica membrane, a organic-inorganic hybrid silica membrane, a zeolitic membrane, and a polymeric membrane which comprises a polyvinyl alcohol, polyimide, chitosan, or mixtures thereof.
3. The apparatus of claim 1 , wherein the pervaporation membrane module is maintained at a temperature within a range of 65 to 200° C.
4. The apparatus of claim 1 , wherein the feed and retentate side of the pervaporation membrane module is maintained at a level equal to 1 to 20 bars.
5. The apparatus of claim 1 , wherein the atmospheric distillation column is maintained at a level equal to 0.5 to 5 bars.
6. The apparatus of claim 1 , wherein the high pressure distillation column is maintained at a level equal to 5 to 20 bars.