Polycarbonate transesterification process

Claim 2

A polycarbonate process comprising contacting in the presence of a base, a β-fluoroaliphatic carbonate, and a polyhydroxy compound selected from alcohols and/or phenols.

Claim 3

A claim 1 process wherein, (A) the β-fluoroaliphatic carbonate contains at least two oxy groups both independently and directly bonded to the same carbonyl carbon atom subject to the proviso that at least one of the oxy groups is separated from at least one fluorine atom by at least two aliphatic carbon atoms; (B) the alcohol is of the formula R a --OH) x , wherein R a represents an aliphatic radical and --OH radicals are attached directly to aliphatic ring carbon atoms, x being a number at least equal to 2; and (C) the phenol is of the formula R b --OH) x , wherein R b represents an aromatic radical and --OH radicals are attached directly to aromatic ring carbon atoms, x being a number at least equal to 2.

Claim 4

The claim 2 process wherein, (B) the alcohol is of the formula C n H 2n+2-z , n is a whole number of from 1-30, and z is a whole number of from 2-4; and (C) the phenol is of the formula ##STR10## wherein R f is an alkylene, alkylidene, cycloalkylene, cycloalkylidene or arylene linkage or a mixture thereof, a linkage selected from the group consisting of ether, carbonyl, amine, a sulfur or phosphorus containing linkage, Ar and Ar' are arene radicals, Y is a substituent selected from the group consisting of organic, inorganic and organometallic radicals, X is halogen or a monovalent hydrocarbon group selected from the class consisting of alkyl, aryl and cycloalkyl and combinations thereof, d represents a whole number of at least 0 up to a maximum equivalent to the number of replaceable hydrogens substituted on the aromatic rings comprising Ar or Ar', e represents a whole number of from 0 to a maximum controlled by the number of replaceable hydrogens on R f , a, b and c represent whole numbers including 0, when b is not zero, neither a or c may be zero, otherwise either a or c but not both may be 0, when b is zero, the aromatic groups can be joined by direct carbon bonds.

Claim 5

The claim 3 process wherein, (C) the phenols are of the formulae ##STR11## where independently each R is hydrogen, chlorine, bromine or a C 1-30 monovalent hydrocarbon or hydroxycarbonoxy group, each Z is hydrogen, chlorine or bromine, subject to the proviso that at least one Z is chlorine or bromine, or ##STR12## where independently each R is as defined hereinbefore, and independently R g and R h are hydrogen or a C 1-30 monovalent hydrocarbon group.

Claim 6

The claim 4 process wherein, (A) the β-fluoroaliphatic carbonates contain from 4-25 carbon atoms.

Claim 7

The claim 5 process wherein, (A) the β-fluoroaliphatic carbonate is selected from ##STR13##

Claim 8

The claim 6 process wherein the process is carried out at a temperature within the range of from 80°-300° C. and within a pressure range including atmospheric to subatmospheric pressures.

Claim 9

The claim 7 process wherein at least a portion of a β-fluoroalkanol is withdrawn from the reaction medium to facilitate the formation of a high molecular weight aromatic polycarbonate.

Claim 10

The claim 8 process wherein the β-fluoroaliphatic carbonate is bis(2,2,2-trifluoroethyl) carbonate and the phenol is bis(4-hydroxyphenyl)propane-2,2.

Claim 11

The claim 9 process wherein the polycarbonate product of the process has a weight average molecular weight of from about 10,000 to about 50,000.