Process for the preparation of (meth)acrylate di-ammonium salts and their use as monomers for the synthesis of polymers
View Patent ↗The invention relates to the preparation of (meth)acrylate di-ammonium salts responding to formula (I) wherein R 1 represents hydrogen or methyl, each R 2 , independently, represents an alkyl comprising from 1 to 4 carbon atoms, each R 3 , independently, represents an alkyl or an aralkyl and each X − , independently, represents an anion; having a high purity and their use as monomers for the synthesis of polymers useful as cationic flocculants.
1. Process for the manufacture of a (meth)acrylate di-ammonium salt of formula (I)
wherein R 1 represents hydrogen or methyl, each R 2 , independently, represents a C1 to C4 alkyl, each R 3 , independently, represents an alkyl or an aralkyl and each X − , independently, represents an anion selected from the group consisting of halides and methylsulfonates, comprising
(1) the reaction of the di-amino (meth)acrylate of formula (II)
with at least one alkyl or aralkyl derivative of formula R 3 X in an aprotic dipolar organic solvent containing at most 5000 ppm of water and wherein the compound of formula (I) has a solubility at 25° C. of less than 1 g/100 g of solvent and wherein the solubility of the corresponding amino-(meth)acrylate ammonium salt of formula (V)
has a solubility at 25° C. of at least 20 g/100 g of solvent; and
(2) the separation of the compound of formula (I) from the reaction mixture without dissolving it in water, the compound of formula (I) being separated from the reaction mixture in the form of a solid product comprising, per mole of the compound of formula (I), less than 0.1 mole of the compound of formula (V).
2. Process for the manufacture of a polymer which process includes the process of claim 1 and comprises the further step (3) of polymerising of at least the compound of formula (I) contained in said solid product to achieve said polymer.
3. Process according to claim 2 , wherein step (3) comprises the co-polymerisation of at least 12% by weight of the compound of formula (I) contained in said solid product with at the most 88% by weight of at least one further monomer.
4. Process according to claim 2 , wherein step (3) comprises a radical co-polymerisation of a water-based solution of monomers polymerised by emulsion or suspension techniques.
5. Process according to claim 2 , wherein step (3) comprises the co-polymerisation of from 1 to 99 parts by moles of the compound of formula (I) contained in said solid product with from 1 to 99 parts by moles of at least one acrylamide monomer of formula (VI)
wherein R 5 is hydrogen or methyl, R 6 and R 7 are, independently, hydrogen, or C1 to C6 alkyl, optionally substituted by one or more hydroxy or alkoxy groups.
6. Process according to claim 1 , wherein the separation of the (meth)acrylate di-ammonium salt of formula (I) from the reaction mixture is done by mechanical separation.
7. Process according to claim 1 , wherein the reaction mixture obtained after step (2) is recycled.
8. Process according to claim 1 , wherein the di-amino (meth)acrylate of formula (II) used in step (1) is prepared by the transesterification of a 1,3-di-amino-2-propanol of formula (III)
wherein each R 2 , independently represents a C1 to C4 alkyl, with a (meth)acrylate of formula (IV)
wherein R 1 represents hydrogen or methyl and R 4 represents a C1 to C4 alkyl, in the presence of a lithium-catalyst.
9. Process according to claim 1 , wherein X is Cl.
10. Process according to claim 1 , wherein the di-amino (meth)acrylate of formula (II) is allowed to react in step (1) with more than 2 equivalents of said alkyl or aralkyl derivative of formula R 3 X.
11. Process according to claim 1 , wherein the reaction of step (1) is effectuated in an amount of between 500 and 5000 g of solvent per mole of the di-amino (meth)acrylate of formula (II).
12. Process according to claim 8 , wherein the lithium catalyst is chosen from Li 2 O, LiOCH 3 , LiOH and their mixtures.
13. Process according to claim 8 , wherein the transesterification is done at a temperature not exceeding 120° C.
14. Process according to claim 1 , wherein R 1 is methyl.
15. Process according to claim 1 , wherein R 2 is methyl.
16. Process according to claim 1 , wherein R 3 is methyl.
17. Process according to claim 1 , wherein R 3 is benzyl.
18. Process according to claim 8 , wherein R 4 in formula (IV) is methyl.
19. Process according to claim 1 , wherein said organic solvent contains at most 1000 ppm of water.
20. Process according to claim 1 , wherein the solubility of the compound of formula (I) in said organic solvent is less than 0.5 g/100 g of solvent.
21. Process according to claim 1 , wherein the solid product which is separated from the reaction mixture comprises, per mole of the compound of formula (I), less than 0.05 mole of the compound of formula (V).
22. Process according to claim 1 , wherein the solid product which is separated from the reaction mixture comprises, per mole of the compound of formula (I), less than 0.01 mole of the compound of formula (V).
23. Process according to claim 1 , wherein the solvent is selected from the group consisting of acetone, methylethylketone, ethylacetate, nitromethane, acetonitrile or mixtures thereof.
24. Process according to claim 23 , wherein the solvent is acetonitrile.
25. Process according to claim 10 , wherein the di-amino (meth)acrylate of formula (II) is allowed to react in step (1) with more than 2.1 equivalents of said alkyl or aralkyl derivative of formula R 3 X.