HIGH FLOW, DUAL-TERMINATED POLYAMIDE POLYMERS
Polyamides terminated at the amine end group, the carboxyl end group, or both the amine and carboxyl end groups. Specifically, the present disclosure relates to terminated polyamide polymers having a weight average molecular weight (Mw) from 22,000 Da to 56,000 Da and a formic acid viscosity (FAV) of less than 45.
1 . A terminated polyamide, comprising:
a weight average molecular weight (Mw) from 22,000 Da to 56,000 Da; and
a formic acid viscosity (FAV) of less than 45.
2 . The terminated polyamide of claim 1 , comprising:
a weight average molecular weight (Mw) from 22,000 Da to 36,000 Da; and
a formic acid viscosity (FAV) of less than 45.
3 . The terminated polyamide of claim 1 , having carboxyl end groups, and wherein a percentage of carboxyl end group termination is from 30 wt. % to 60 wt. %.
4 . The terminated polyamide of claim 1 , having amine end groups, and wherein a percentage of amine end group termination is from 30 wt. % to 50 wt. %.
5 . The terminated polyamide of claim 1 , wherein the terminated polyamide has a relative viscosity (RV) of 2.0 to 2.6.
6 . The terminated polyamide of claim 1 , wherein the terminated polyamide has a melt flow index (MFI) from 20 g/10 min to 40 g/10 min.
7 . The terminated polyamide of claim 1 , wherein the ratio of the weight average molecular weight (Mw) of the terminated polyamide to the number average molecular weight (Mn) of the terminated polyamide is from 1.8 to 3.5.
8 . The terminated polyamide of claim 1 , further comprising glass fibers in an amount from 30 wt. % to 40 wt. %, based on the combined weight of the terminated polyamide and glass fibers.
9 . A process of synthesizing a terminated polyamide, comprising:
hydrolyzing a lactam to provide monomers having an amine end group and a carboxyl end group;
polycondensing the monomers at a temperature of 230° C. to 270° C. to provide polyamide polymers having an amine end group and a carboxyl group; and
terminating the polyamide by reaction with at least one chain terminator to provide a terminated polyamide with a weight average molecular weight (Mw) of 22,000 Da to 56,000 Da and a formic acid viscosity (FAV) of less than 45.
10 . The process of claim 9 , wherein the terminated polyamide has a weight average molecular weight of 22,000 Da to 36,000 Da and a formic acid viscosity (FAV) of less than 45.
11 . The process of claim 9 , wherein the chain terminators are selected from the group consisting of cyclohexylamine, stearylamine, stearic acid, and acetic acid.
12 . The process of claim 9 , wherein the percentage of carboxyl end group termination of the terminated polyamide is from 30 wt. to 60 wt. %.
13 . The process of claim 9 , wherein the percentage of amine end group termination of the terminated polyamide is from 30 wt. % to 50 wt. %.
14 . The process of claim 9 , further comprising the addition of glass fibers in an amount from 30 wt. % to 40 wt. %, based on a combined weight of the polyamide and glass fibers to provide a glass filled polyamide.
15 . A polyamide composition comprising:
the glass filled polyamide of claim 14 in an amount from 80 wt. % to 90 wt. %, based on a total weight of the composition; and
a second polyamide in an amount from 10 wt. % to 20 wt. %, based on a total weight of the composition.
16 . The composition of claim 15 , wherein the second polyamide is selected from the group consisting of unterminated polyamides and dual terminated polyamides.
17 . The composition of claim 15 , wherein the melt flow index (MFI) of the composition is from 30 g/10 min to 45 g/10 min.
18 . The composition of claim 15 , wherein the ratio of the weight average molecular weight (Mw) of the terminated polyamide to the number average molecular weight (Mn) of the terminated polyamide is 1.8 to 3.5.