Method for producing butanediol dimethacrylates
View Patent ↗The present invention relates to a process for preparing butanediol dimethacrylates, which comprises the transesterification of butanediol with an ester of methacrylic acid in the presence of catalysts, wherein a combination comprising at least one lithium compound and at least one calcium compound is used as catalyst, at least one of the compounds of lithium and/or of calcium is an oxide, a hydroxide, an alkoxide having from 1 to 4 carbon atoms or a carboxylate having from 1 to 4 carbon atoms and at least part of the reaction is carried out in the presence of an effective amount of water. The process of the invention makes a particularly inexpensive preparation of butanediol dimethacrylates having a very high purity possible.
1. A process for preparing a butanediol dimethacrylate, comprising:
transesterifying butanediol with an ester of methacrylic acid in the presence of a catalyst,
wherein a combination comprising at least one lithium compound and at least one calcium compound is used as catalyst, at least one of the compounds of lithium and/or of calcium is an oxide, a hydroxide, an alkoxide having from 1 to 4 carbon atoms or a carboxylate having from 1 to 4 carbon atoms and at least part of the reaction is carried out in the presence of an effective amount of water;
wherein the effective amount of water, based on the weight of the butanediol used, is in the range from 0.01 to 4% by weight.
2. The process according to claim 1 , wherein 1,4-butanediol is used.
3. The process according to claim 1 , wherein 1,3-butanediol is used.
4. The process according to claim 1 , wherein water is added to the reaction mixture.
5. The process according to claim 1 , wherein the amount of water, based on the weight of the butanediol used, is in the range from 0.1 to 1% by weight.
6. The process according to claim 1 , wherein the ratio of the weight of water to the weight of the catalyst is in the range from 5:1 to 1:5.
7. The process according to claim 1 , wherein the ratio of the weight of water to the weight of the lithium compound is in the range from 20:1 to 1:1.
8. The process according to claim 1 , wherein the ratio of the weight of water to the weight of the calcium compound is in the range from 10:1 to 1:2.
9. The process according to claim 1 , wherein lithium hydroxide, lithium oxide, lithium methoxide and/or lithium ethoxide is used as the lithium compound.
10. The process according to claim 1 , wherein calcium oxide, calcium hydroxide, calcium methoxide and/or calcium ethoxide is used as the calcium compound.
11. The process according to claim 1 , wherein a mixture comprising lithium hydroxide and calcium oxide is used as the catalyst.
12. The process according to claim 1 , wherein a mixture comprising lithium hydroxide and calcium hydroxide is used as the catalyst.
13. The process according to claim 1 , wherein the ratio of the weight of the lithium compound to the weight of the calcium compound is in the range from 20:1 to 1:20.
14. The process according to claim 13 , wherein the ratio of the weight of the lithium compound to the weight of the calcium compound is in the range from 1:1 to 1:10.
15. The process according to claim 1 , wherein the reaction time is in the range from 2 to 20 hours.
16. The process according to claim 15 , wherein the reaction time is in the range from 6 to 12 hours.
17. The process according to claim 1 , wherein methyl methacrylate is used as the ester of methacrylic acid.
18. The process according to claim 1 , wherein ethyl methacrylate is used as the ester of methacrylic acid.
19. The process according to claim 1 , wherein the weight ratio of butanediol to the ester of methacrylic acid is in the range from 1:2 to 1:20.
20. The process according to claim 19 , wherein the weight ratio of butanediol to the ester of methacrylic acid is in the range from 1:3 to 1:10.
21. The process according to claim 1 , wherein the reaction is carried out at a pressure in the range from 500 to 1300 mbar.
22. The process according to claim 1 , wherein the reaction is carried out at a temperature in the range from 90° C. to 130° C.
23. The process according to claim 1 , wherein the temperature at which the reaction occurs is increased during the course of the reaction.
24. The process according to claim 22 , wherein the temperature at the beginning of the reaction is in the range from 90° C. to 110° C. and that towards the end of the reaction is in the range from 115° C. to 130° C.
25. The process according to claim 1 , wherein the reaction is carried out in the presence of a polymerization inhibitor.
26. The process according to claim 25 , wherein a phenol is used as the polymerization inhibitor.
27. The process according to claim 1 , wherein the reaction is carried out with the introduction of oxygen.
28. The process according to claim 1 , wherein the alcohol liberated from the ester of methacrylic acid used is separated off by distillation.
29. The process according to claim 28 , wherein methanol or ethanol is separated off.
30. The process according to claim 28 , wherein a mixture containing methyl methacrylate and methanol is separated off.
31. The process according to claim 28 , wherein part of the mixture which has been separated off is recirculated to the following batch.
32. The process according to claim 31 , wherein the proportion which is recirculated of the mixture which has been separated off is obtained at the end of the reaction.
33. The process according to claim 1 , wherein methyl methacrylate is added during the transesterification.
34. The process according to claim 33 , wherein the weight ratio of the amount of methyl methacrylate added during the transesterification to the amount of methanol/methyl methacrylate mixture separated off is in the range from 2:1 to 1:3.