PROCESS FOR CONTINUOUSLY PREPARING DIALKYL CARBONATE
The present invention relates to a process comprising purifying dialkyl carbonates of the formula (II) in one or more columns in the presence of an alkylene oxide of the formula (V) and of an alkyl alcohol of the formula (IV) wherein R 1 and R 2 represent, independently of one another, linear or branched, substituted or unsubstituted C 1 -C 6 -alkyl, R 3 and R 4 represent, independently of one another, hydrogen, substituted or unsubstituted C 1 -C 4 -alkyl, substituted or unsubstituted C 2 -C 4 -alkenyl or substituted or unsubstituted C 6 -C 12 -aryl, and R 5 represents a straight-chain or branched C 1 -C 4 -alkyl; and wherein the mean residence time of the dialkyl carbonate in the column(s) is from 0.3 h to 3 h.
1 . A process comprising purifying dialkyl carbonates of the formula (II) in one or more columns in the presence of an alkylene oxide of the formula (V) and of an alkyl alcohol of the formula (IV)
wherein R 1 and R 2 represent, independently of one another, linear or branched, substituted or unsubstituted C 2 -C 6 -alkyl,
R 3 and R 4 represent, independently of one another, hydrogen, substituted or unsubstituted C 1 -C 4 -alkyl, substituted or unsubstituted C 2 -C 4 -alkenyl or substituted or unsubstituted C 6 -C 12 -aryl, and
R 5 represents a straight-chain or branched C 1 -C 4 -alkyl; and
wherein the mean residence time of the dialkyl carbonate in the column(s) is from 0.3 h to 3 h.
2 . The process according to claim 1 , wherein the mean residence time of the dialkyl carbonate in the column(s) is from 0.5 h to 2 h.
3 . The process according to claim 1 , wherein the alcohol comprises methanol or ethanol.
4 . The process according to claim 2 , wherein the alcohol comprises methanol or ethanol.
5 . The process according to any of claim 1 , wherein the alkylene comprises ethylene or propylene.
6 . The process according to any of claim 4 , wherein the alkylene comprises ethylene or propylene.
7 . The process according to claim 1 , wherein the pressure in at least one of the columns used for purification of the dialkyl carbonate is from 0.5 to 50 bar absolute.
8 . The process according to claim 6 , wherein the pressure in at least one of the columns used for purification of the dialkyl carbonate is from 0.5 to 50 bar absolute.
9 . The process according to claim 1 , wherein the pressure in at least one of the columns used for purification of the dialkyl carbonate is from 2 to 20 bar absolute.
10 . The process according to claim 8 , wherein the pressure in at least one of the columns used for purification of the dialkyl carbonate is from 2 to 20 bar absolute.
11 . The process according to claim 1 , wherein the temperature in at least one of the columns used for purification of the dialkyl carbonate is from 120° C. to 210° C.
12 . The process according to claim 10 , wherein the temperature in at least one of the columns used for purification of the dialkyl carbonate is from 120° C. to 210° C.
13 . The process according to claim 1 , wherein at least one of the columns used for purification of the dialkyl carbonate is a packed column.
14 . The process according to claim 12 , wherein at least one of the columns used for purification of the dialkyl carbonate is a packed column.