GREENER METHOD FOR THE PRODUCTION OF COPOLYMER 1
The present invention provides a greener method for the production of polyamino acid random copolymers containing alanine, glutamic acid, lysine and tyrosine. In particular, the present invention provides a greener method for the production of Copolymer 1 or a pharmaceutically acceptable salt thereof via a synthetic route that only requires a single deprotection step.
1 . A method for the production of a polyamino acid random copolymer comprising tyrosine, alanine, glutamic acid, and lysine, the method comprising:
(a) polymerizing a mixture of N-carboxyanhydride of tyrosine, N-carboxyanhydride of alanine, N-carboxyanhydride of R 1 protected glutamic acid, N-carboxyanhydride of a base-labile protected lysine in the presence of a polymerization initiator to form a protected polyamino acid random copolymer; wherein R 1 is an alkyl; and
(b) adding a base to the protected polyamino acid random copolymer of step (a) to form the polyamino acid random copolymer or a pharmaceutically acceptable salt thereof, wherein the base cleaves R 1 from the glutamic acid residue and the base-labile protecting group from the lysine residue.
2 . The method of claim 1 , wherein the polymerization initiator is a nucleophile.
3 . The method of claim 2 , wherein the nucleophile is chosen from a metal alkoxide and an amine.
4 . The method of claim 1 , wherein the molar ratio of the N-carboxyanhydrides to the polymerization initiator in step (a) is from about 5:1 to about 1,000:1.
5 . The method of claim 1 , wherein the polymerization reaction of step (a) is carried out in the presence of a solvent chosen from dioxane, chloroform, dichloromethane, acetonitrile, and combinations thereof, and the reaction is conducted at a temperature ranging from about 20° C. to about 40° C.
6 . The method of claim 1 , wherein R 1 is chosen from methyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, tert-butyl, straight pentyl, and branched pentyl.
7 . The method of claim 1 , wherein R 1 is ethyl.
8 . The method of claim 1 , wherein the base-labile protecting group is chosen from TFA and Fmoc.
9 . The method of claim 1 , wherein R 1 is ethyl and the base-labile protecting group is TFA.
10 . The method of claim 1 , wherein the base of step (b) is selected from the group consisting of sodium hydroxide, potassium hydroxide, rubidium hydroxide, and combinations thereof.
11 . The method of claim 1 , wherein the reaction of step (b) is carried out in the presence of an alcoholic solvent at a temperature ranging from about 15° C. to about 30° C.
12 . The method of claim 1 , wherein the polyamino acid random copolymer has a mass-average molecular weight of about 2000 to about 100,000.
13 . The method of claim 1 , wherein the polyamino acid random copolymer has a mass-average molecular weight of about 5000 to about 10,000.
14 . The method of claim 1 , wherein the ratio of alanine to glutamic acid to lysine to tyrosine present in the polyamino acid random copolymer is about 5:1:4:1 to about 7:3:6:1.
15 . The method of claim 1 , wherein the ratio of alanine to glutamic acid to lysine to tyrosine present in the polyamino acid random copolymer is about 6:2:5:1.
16 . The method of claim 1 , wherein the yield of the polyamino acid random copolymer is at least 70%.
17 . The method of claim 1 , wherein the optical purity of the polyamino acid random copolymer is at least 99%.
18 . The method of claim 1 , wherein the amino acids comprising the polyamino acid random copolymer are at each occurrence in a D or an L configuration.
19 . The method of claim 1 , wherein the polyamino acid random copolymer is a pharmaceutically acceptable salt chosen from metal salts, inorganic and organic acid salts.
20 . The method of claim 1 , wherein the polyamino acid random copolymer is an acetate salt.
21 . The method of claim 1 , wherein the polyamino acid random copolymer is Copolymer 1.
22 . The method of claim 1 , wherein the polymerization initiator is a nucleophile chosen from a metal alkoxide and an amine; the molar ratio of the N-carboxyanhydrides to the polymerization initiator in step (a) is from about 5:1 to about 1,000:1; the polymerization reaction of step (a) is carried out in the presence of a solvent chosen from dioxane, chloroform, dichloromethane, acetonitrile, and combinations thereof, and the reaction is conducted at a temperature ranging from about 20° C. to about 40° C.; the base of step (b) is selected from the group consisting of sodium hydroxide, potassium hydroxide, rubidium hydroxide, and combinations thereof; and the reaction of step (b) is carried out in the presence of an alcoholic solvent at a temperature ranging from about 15° C. to about 30° C.