Method for producing ethylene glycol dimethacrylate

1. A process for preparing ethylene glycol dimethacrylate, comprising transesterifying ethylene glycol with an ester of methacrylic acid in a reaction mixture comprising at least one catalyst, wherein said catalyst comprises lithium amide (LiNH 2 ) and lithium chloride (LiCl).

2. The process according to claim 1 , further comprising adding additional lithium amide to the reaction mixture during said transesterifying.

3. The process according to claim 1 , wherein the weight ratio of lithium amide to lithium chloride is in the range of from 20:1 to 1:20.

4. The process according to claim 3 , wherein the weight ratio of lithium amide to lithium chloride is in the range of from 5:1 to 1:1.

5. The process according to claim 1 , wherein said transesterifying is carried out for a reaction time of from 5 to 20 hours.

6. The process according to claim 5 , wherein said transesterifying is carried out for a reaction time of from 6 to 12 hours.

7. The process according to claim 1 , wherein the ester of methacrylic acid is methyl methacrylate.

8. The process according to claim 1 , wherein the ester of methacrylic acid is ethyl methacrylate.

9. The process according to claim 1 , wherein the weight ratio of ethylene glycol to the ester of methacrylic acid is in the range of from 1:2 to 1:20.

10. The process according to claim 9 , wherein the weight ratio of ethylene glycol to the ester of methacrylic acid is in the range of from 1:5 to 1:15.

11. The process according to claim 1 , wherein said transesterifying is carried out at a pressure in the range of from 200 to 2000 mbar.

12. The process according to claim 1 , wherein said transesterifying is carried out at a temperature in the range of from 90° C. to 130° C.

13. The process according to claim 1 , wherein the temperature at which said transesterifying occurs is increased during the course of the reaction.

14. The process according to claim 12 , wherein a temperature at the beginning of said transesterifying is in the range from 90° C. to 110° C. and a temperature at the end of said transesterifying is in the range from 115° C. to 130° C.

15. The process according to claim 1 , wherein said transesterifying is carried out in the presence of a polymerization inhibitor.

16. The process according to claim 15 , wherein the polymerization inhibitor is an amine.

17. The process according to claim 1 , wherein said transesterifying further comprises introducing oxygen to the reaction mixture.

18. The process according to claim 1 , further comprising distilling the alcohol liberated from the ester of methacrylic acid to separate the alcohol from the reaction mixture.

19. The process according to claim 18 , further comprising separating methanol or ethanol from the reaction mixture.

20. The process according to claim 18 , further comprising separating a mixture containing methyl methacrylate and methanol from the reaction mixture.

21. The process according to claim 18 , further comprising recirculating the alcohol which has been separated from the reaction mixture into a following batch.

22. The process according to claim 21 , wherein the alcohol which is recirculated is obtained at the end of the reaction.

23. The process according to claim 20 , further comprising adding methyl methacrylate to the reaction mixture during said transesterifying.

24. The process according to claim 23 , wherein the weight ratio of the amount of the methyl methacrylate added to the reaction mixture during said transesterifying to the amount of the mixture containing methyl methacrylate and methanol which is separated is in the range from 2:1 to 1:2.

25. The process according to claim 19 , further comprising recirculating the methanol or ethanol which has been separated from the reaction mixture into a following batch.

26. The process according to claim 20 , further comprising recirculating the mixture containing methyl methacrylate and methanol which has been separated from the reaction mixture into a following batch.