Process for preparing diaryl alkylphosphonates and oligomeric/polymeric derivatives thereof
A process is provided for the production of diaryl alkyl phosphonate by the reaction of triaryl phosphate with dialkyl alkyl phosphonate in the presence of alkali metal iodide catalyst; and, optionally, the diaryl alkyl phosphonate is reacted in situ with aromatic diol and, optionally, with at least one branching monomer, in the absence of other or further added catalyst to provide oligomeric and/or polymeric phosphonate products.
1. A process for preparing arylene alkylphosphonate oligomer and/or polymer which comprises:
a) reacting triaryl phosphite with dialkyl alkylphosphonate in the presence of a catalytically effective amount of catalyst of the formula MXn in which M is an alkali metal or alkaline earth metal, X is iodine or bromine and n is equal to the valence of M, optionally, in a closed reactor, to provide diaryl alkylphosphonate; and,
b) reacting the diaryl alkylphosphonate with aromatic diol and, optionally, at least one branching monomer, in the absence of other or further added catalyst to provide the arylene alkylphosphonate oligomer and/or polymer.
2. The process of claim 1 wherein the diaryl alkylphosphonate of step (a) is reacted without removal of catalyst therefrom with the aromatic diol.
3. The process of claim 1 wherein in step (a) the triaryl phosphite is triphenyl phosphite, the dialkyl alkylphosphonate is dimethyl methylphosphonate, in catalyst MXn, M is sodium, X is iodine and n is equal to 1, the catalyst is present at from about 0.01 to about 0.5% by weight diaryl alkylphosphonate is diphenyl methylphosphonate, and in step (b) the aromatic diol is resorcinol and the arylene alkylphosphonate oligomer and/or polymer is resorcinol methylphosphonate oligomer and/or polymer.
4. The process of claim 3 wherein the diaryl alkylphosphonate of step (a) is reacted without removal of catalyst therefrom with the aromatic diol.
5. The process of claim 1 in which the mole ratio of aromatic diol to diaryl alkyl phosphonate is greater than 1 and the arylene alkylphosphonate oligomer and/or polymer possesses at least one terminal hydroxyl group.
6. The process of claim 2 in which the mole ratio of aromatic diol to diaryl alkyl phosphonate is greater than 1 and the arylene alkylphosphonate oligomer and/or polymer possesses at least one terminal hydroxyl group.
7. The process of claim 3 in which the mole ratio of aromatic diol to diaryl alkyl phosphonate is greater than 1 and the arylene alkylphosphonate oligomer and/or polymer possesses at least one terminal hydroxyl group.
8. The process of claim 4 in which the mole ratio of aromatic diol to diaryl alkyl phosphonate is greater than 1 and the arylene alkylphosphonate oligomer and/or polymer possesses at least one terminal hydroxyl group.
9. The process of claim 1 wherein the arylene alkylphosphonate oligomer and/or polymer has a number average molecular weight of from about 800 to about 5,000.
10. The process of claim 1 wherein the arylene alkylphosphonate oligomer and/or polymer has a number average molecular weight of from about 1,000 to about 2,500.
11. The process of claim 3 wherein the arylene alkylphosphonate oligomer and/or polymer has a number average molecular weight of from about 800 to about 5,000.
12. The process of claim 3 wherein the arylene alkylphosphonate oligomer and/or polymer has a number average molecular weight of from about 1,000 to about 2,500.
13. The process of claim 5 wherein the arylene alkylphosphonate oligomer and/or polymer has a number average molecular weight of from about 800 to about 5,000.
14. The process of claim 5 wherein the arylene alkylphosphonate oligomer and/or polymer has a number average molecular weight of from about 1,000 to about 2,500.
15. The process of claim 7 wherein the arylene alkylphosphonate oligomer and/or polymer has a number average molecular weight of from about 800 to about 5,000.
16. The process of claim 7 wherein the arylene alkylphosphonate oligomer and/or polymer has a number average molecular weight of from about 1,000 to about 2,500.