Process for preparing dialkyl carbonates from alkylene carbonates and alcohols
The present invention relates to a continuous process for preparing lower dialkyl carbonates as main product and alkylene glycol as by-product by catalyzed transesterification of a cyclic alkylene carbonate (e.g. ethylene carbonate or propylene carbonate) with lower alcohols, where the reaction of the alkylene carbonate is carried out with an alcohol containing dialkyl carbonate in countercurrent, characterized in that introduction of a stream containing at least 99.5% by weight of alcohol takes place below the point of introduction for the alcohol containing dialkyl carbonate in a particular spacing ratio between the abovementioned points of introduction.
1. A process for continuously preparing a dialkyl carbonate of formula (I)
(R 1 O) 2 CO (I)
wherein
R 1 is straight-chain or branched C 1 -C 4 alkyl group,
and
an alkylene glycol of formula (II)
R 2 (OH) 2 (II)
wherein
R 2 is a C 2 -C 4 -alkyl group,
as by-product
comprising reacting
a cyclic alkylene carbonate having the following formula:
wherein
R 2 is a C 2 -C 4 -alkyl group,
with
an alcohol of formula (III)
R 1 OH (III)
wherein
R 1 is straight-chain or branched C 1 -C 4 alkyl group,
in the presence of a catalyst,
wherein said reaction is carried out in countercurrent in a column, wherein said reaction comprises the steps of
(A) introducing said cyclic alkylene carbonate as a stream into the upper part of said column at point (1),
(B) introducing said alcohol of formula (III), which comprises said dialkyl carbonate of formula (I), as a stream into the middle or lower part of said column at point (3), and
(C) introducing a stream comprising said alcohol of formula (III) as a stream into said column at a point (4) on said column below point (3),
wherein the ratio of the spacing between point (1) and point (3) to the spacing between point (1) and point (4) is in the range of from 0.20 to 0.52.
2. The process of claim 1 , wherein the ratio of the spacing between point (1) and point (3) to the spacing between point (1) and point (4) is in the range of from 0.28 to 0.44.
3. The process of claim 1 , wherein the dialkyl carbonate of formula (I) content of said alcohol of formula (III) comprising said dialkyl carbonate of formula (I) is in the range of from 0.2 to 30% by weight.
4. The process of claim 1 , wherein said cyclic alkylene carbonate is ethylene carbonate or propylene carbonate.
5. The process of claim 1 , wherein said alcohol of formula (III) is methanol and said dialkyl carbonate of formula (I) is dimethyl carbonate.
6. The process of claim 1 , wherein the proportion by weight of said cyclic alkylene carbonate in said stream is maintained below 1000 ppm.
7. The process of claim 1 , wherein the proportion by weight of said cyclic alkylene carbonate in said stream is maintained below 500 ppm.
8. The process of claim 1 , wherein said stream introduced at point (4) is an alcohol having a purity of at least 90% by weight.
9. The process of claim 1 , wherein said stream introduced at point (4) is an alcohol having a purity of at least 95% by weight.
10. The process of claim 1 , wherein said stream introduced at point (4) is an alcohol having a purity of at least 99.5% by weight.
11. The process of claim 1 , wherein said catalyst is a homogeneous catalyst.
12. The process of claim 1 , wherein said catalyst is potassium hydroxide or sodium hydroxide.
13. The process of claim 1 , wherein said column comprises at least one enrichment section in the upper part of said column and at least one reaction zone below said at least one enrichment section.
14. The process of claim 1 , wherein said column comprises at least one stripping section below a reaction zone.
15. The process of claim 1 , wherein said column comprises at least one reaction zone, wherein the temperature of said at least one reaction zone is in the range from 20 to 200° C. and the pressure at the top of said column is in the range from 0.4 to 5 bar.
16. The process of claim 1 , wherein said cyclic alkylene carbonate and said alcohol of formula (III) are used in a molar ratio of from 1:2.0 to 1:20.