Method for purifying crude cyclic ester
A purification method and technology of cyclic esters, which are applied in the field of purification of crude cyclic esters, can solve the problems of complex purification process, poor purification effect, high energy consumption, etc., and achieve the effects of increasing yield, reducing energy consumption, and reducing the number of operations
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0044] (1) Mix crude glycolide with recrystallization solvent I ethyl acetate and recrystallization solvent II ethanol, and perform one recrystallization to obtain glycolide crystals, wherein the volume ratio of ethyl acetate and ethanol is 1:0.5; In the obtained glycolide crystal, the content of reaction solvent nitrobenzene is 0.1wt%, the content of free acid acetic acid is 0.4wt%, the content of oligomer polyglycolic acid is 0.9wt%, and the content of recrystallization solvent is 1.2wt%. wt%, the content of glycolide is 97.4wt%;
[0045] (2) Glycolide crystals are transported into a cyclic ester melting tank to form molten glycolide under normal pressure and 86° C., and flush into nitrogen to seal to prevent the oxidation of molten glycolide; The molten material enters the evaporator from the top of the wiped film evaporator for variable temperature evaporation, wherein the pressure of the wiped film evaporator is 2kPaA, the low temperature evaporation temperature at the up...
Embodiment 2
[0048] (1) recrystallize crude lactide and recrystallization solvent I butyl acetate once to obtain lactide crystals, wherein, in the obtained lactide crystals, the content of the reaction solvent dimethylformamide is 0.16wt% , the content of free acid acetic acid is 0.56wt%, the content of oligomer polylactic acid is 0.88wt%, the content of recrystallization solvent is 1.1wt%, and the content of lactide is 97.3wt%;
[0049] (2) Lactide crystals are transported into a cyclic ester melting tank, and molten lactide is formed under normal pressure and 102° C., and then flushed into nitrogen to seal to prevent the oxidation of lactide in the molten state; The molten material enters the evaporator from the top of the wiped film evaporator for variable temperature evaporation, wherein the pressure of the wiped film evaporator is 20kPaA, the low temperature evaporation temperature at the upper part of the heat exchange tube of the wiped film evaporator is 104°C, and the residence time...
Embodiment 3
[0052] (1) Mix crude lactide with recrystallization solvent I methyl acetate and recrystallization solvent II isopropanol, and perform one recrystallization to obtain lactide crystals, wherein, recrystallization solvent I methyl acetate and recrystallization solvent The volume ratio of II isopropanol is 1:0.8; In the lactide crystal obtained, the content of reaction solvent dimethylformamide is 0.13wt%, the content of free acid acetic acid is 0.1wt%, and the content of oligomer polylactic acid The content is 0.8wt%, the content of recrystallization solvent is 0.9wt%, and the content of lactide is 98.07wt%;
[0053] (2) Transport the lactide crystals to the cyclic ester melting tank, form the molten lactide under the condition of normal pressure and 98° C., and rush into the nitrogen seal to prevent the oxidation of the lactide in the molten state; The molten material enters the evaporator from the top of the wiped film evaporator for variable temperature evaporation. The press...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
