Polyimide molding resins and molded articles

Claim 2

In a solid particulate polyimide, the polyimide having the recurring unit ##STR6## wherein R is a tetravalent radical containing at least one 6-carbon atom ring characterized by benzenoid unsaturation and wherein the four carbonyl groups are attached directly to different carbon atoms in the radical and wherein each pair of carbonyl groups is attached to adjacent carbon atoms in a 6-membered benzenoid ring of the radical and wherein R' is a divalent radical containing at least one six-carbon atom ring, each ring characterized by benzenoid unsaturation, and when at least two rings are present in R', no more than one of the valence bonds is located on any one of the rings, said particles having a surface area of greater than 20 square meters per gram, the improvement wherein the polyimide exhibits a Crystallinity Index of less than about 15, as measured by X-ray diffraction.

Claim 3

A molded article of the polyimide of claim 1 having a density of at least about 1.30 g/cc and containing less than about 2% filler and whicb exhibits a tensile elongation of greater than about 20% and a tensile strength of greater than about 12 kpsi.

Claim 4

A molded article of the polyimide of claim 1 having a density of at least about 1.30 g/cc and containing less than about 10% filler and which exhibits a tensile elongation of greater than about 18% and a tensile strength of greater than about 11.5 kpsi.

Claim 5

A molded article of the polyimide of claim 1 having a density of at least about 1.30 g/cc and containing less than about 50% filler and which exhibits a tensile elongation of greater than about 4% and a tensile strength of greater than about 7 kpsi.

Claim 6

A molded article of claim 2 wherein the filler is graphite.

Claim 7

In a process for the preparation of a solid particulate polyimide by the reaction of (1) at least one organic diamine of the formula H 2 N--R'--NH 2 , wherein R' is a divalent radical containing at least one six-carbon atom ring, each ring characterized by benzenoid unsaturation, and, when at least two rings are present in R', no more than one valence bond is located on any one of said rings, and (2) at least one tetracarboxylic acid dianhydride and converting the resulting product to polyimide, the improvement which comprises: (a) reacting the diamine and the dianhydride in a solvent having a pH of about from 8.0 to 10.0; (b) maintaining the concentration of the solution resulting from the reaction of the tetracarboxylic acid dianhydride and the organic diamine at about from 1 to 15% polymer; (c) bringing the polymer solution into contact with a nonsolvent for the resulting polymer at a temperature of about from 0° to 65° C.; (d) maintaining the ratio of the nonsolvent and original polymer solvent such that the combined solvent and nonsolvent contains no more than about 70% solvent; and (e) agitating the mixture of polymer solution and nonsolvent to bring the nonsolvent and the solution into intimate contact so as to provide a surface area in the polyimide resin of greater than about 20 square meters per gram.

Claim 8

In a process for the preparation of a solid particulate polyimide by the reaction of (1) at least one organic diamine of the formula H 2 N--R'--NH 2 , wherein R' is a divalent radical containing at least one six-carbon atom ring, each ring characterized by benzenoid unsaturation, and, when at least two rings are present in R', no more than one valence bond is located on any one of said rings, and (2) at least one tetracarboxylic acid dianhydride and converting the resulting product to polyimide, the improvement which comprises: (a) reacting the diamine and the dianhydride in a solvent having a pH of about from 8.0 to 10.0; (b) maintaining the concentration of the solution resulting from the reaction of the tetracarboxylic acid dianhydride and the organic diamine at about from 1 to 15% polymer; (c) bringing the polymer solution into contact with a nonsolvent for the resulting polymer at a temperature of about from 0° to 65° C.; (d) maintaining the ratio of the nonsolvent and original polymer solvent such that the combined solvent and nonsolvent contains no more than about 70% solvent; and (e) agitating the mixture of polymer solution and nonsolvent to bring the nonsolvent and the solution into intimate contact so as to provide a surface area in the polyimide resin of greater than about 20 square meters per gram.

Claim 9

A process of claim 6 wherein the concentration of the solution resulting from the reaction of the tetracarboxylic acid dianhydride and the organic diamine is maintained at about from 1 to 10% polymer.

Claim 10

A process of claim 6 wherein the solvent is pyridine.

Claim 11

A process of claim 6 wherein the solvent is β-picoline.

Claim 12

A process of claim 6 wherein the concentration of the solution resulting from the tetracarboxylic acid dianhydride and the organic diamine is less than about 10%.

Claim 13

A process of claim 6 wherein the polymer solution is brought into contact with the nonsolvent at a temperature of about from 10° C. to 40° C.