MELT POLYMERIZATION METHOD FOR POLYETHERIMIDES
A method of making a polyetherimide includes forming a monomer mixture comprising a bis(ether anhydride), a diamine and a volatile organic solvent; removing the volatile organic solvent to form a particulate solid; and melt polymerizing the particulate solid at a temperature 50 to 225° C. greater than the glass transition temperature of the polyetherimide in a single melt mixing device. The polyetherimide has an anhydride-amine stoichiometry and the standard deviation of anhydride-amine stoichiometry is less than 0.4 mol %.
1 . A method of making a polyetherimide comprises forming a monomer mixture comprising a bis(ether anhydride), a diamine and a volatile organic solvent; removing the volatile organic solvent to form a particulate solid; and melt polymerizing the particulate solid at a temperature of 50 to 225° C. higher than the glass transition temperature of the polyetherimide in a single melt mixing device to produce a polyetherimide having an anhydride-amine stoichiometry and the standard deviation of anhydride-amine stoichiometry is less than 0.4 mol %.
2 . The method of claim 1 , wherein the monomer mixture is formed by combining a bis(ether anhydride) mixture and a diamine mixture, wherein the bis(ether anhydride) mixture comprises the bis(ether anhydride) and the volatile organic solvent and the diamine mixture comprises the diamine and the volatile organic solvent.
3 . The method of claim 2 , wherein the bis(ether anhydride) mixture further comprises a chain stopper.
4 . The method of claim 2 , wherein the diamine mixture further comprises a chain stopper.
5 . The method of claim 1 , wherein at least a portion of the melt polymerization is conducted at a pressure below atmospheric pressure (760 mm Hg or 101,325 Pa).
6 . The method of claim 1 , wherein an excess of bis(ether anhydride) relative to the diamine is used to produce a polyetherimide having an excess of anhydride groups relative to the amount of amine groups.
7 . The method of claim 1 , wherein the volatile organic solvent comprises dichloromethane, chloroform, or a combination of the foregoing.
8 . The method of claim 1 , wherein melt polymerizing occurs at a temperature 50 to 150° C. greater than the glass transition temperature of the polyetherimide.
9 . The method of claim 1 , wherein at least a portion of the melt polymerization is conducted at a pressure less than or equal to 5,000 Pa.
10 . The method of claim 1 , wherein the bis(ether anhydride) comprises 2,2-bis[4-(3,4-dicarboxyphenoxy)phenyl]propane dianhydride.
11 . The method of claim 1 , wherein the diamine comprises m-phenylenediamine, p-phenylenediamine, 4,4′-diaminodiphenyl sulfone, 3,4′-diaminodiphenyl sulfone, 3,3′-diaminodiphenyl sulfone, or a combination comprising at least one of the foregoing.
12 . The method of claim 1 , wherein the particulate solid has a solvent content less than or equal to 1000 ppm.
13 . A melt polymerized polyetherimide having anhydride-amine stoichiometry wherein the standard deviation of anhydride-amine stoichiometry is less than 0.4 mol % and a solvent content less than 50 ppm.
14 . The polyetherimide of claim 13 , wherein the polyetherimide has an anhydride-amine stoichiometry of −1 to 2.5 mol %.
15 . The polyetherimide of claim 13 , wherein the polyetherimide has a chlorine content less than or equal to 50 ppm.
16 . The polyetherimide of claim 13 , wherein the polyetherimide has a change in melt viscosity of less than or equal to 50% after being maintained for 30 minutes at 390° C. wherein melt viscosity is determined by ASTM D4440.
17 . The polyetherimide of claim 13 comprising structural units derived from 2,2-bis[4-(3,4-dicarboxyphenoxy)phenyl]propane dianhydride and one or more diamines comprising m-phenylenediamine, p-phenylenediamine, 4,4′-diaminodiphenyl sulfone, 3,4′-diaminodiphenyl sulfone, or 3,3′-diaminodiphenyl sulfone.