Melt-polymerization process for the preparation of thermoplastic polyamides and polyesteramides

Claim 2

A process for the preparation, in the absence of inert organic solvent, of a thermoplastic polymer which is characterized by a recurring amide linkage which process comprises the steps of: intimately mixing an organic diisocyanate and a dicarboxylic acid in substantially stoichiometric proportions; subjecting the reaction mixture to a temperature in the range of about 100° C. to about 230° C. until from about 25 to about 95 percent of the theoretical amount of carbon dioxide necessary to achieve complete reaction has been evolved; and completing the formation of the thermoplastic polymer by melting the intermediate so formed and homogenizing and degassing the melt at a temperature in the range of above about 230° C. but below that at which degradation of the polymer occurs.

Claim 3

A process according to claim 1 wherein the homogenizing of the melt is achieved by extrusion of the polymer.

Claim 4

A process according to claim 1 in which the heating of the initial reaction mixture is continued until at least 50 percent of the theoretical amount of carbon dioxide has been evolved.

Claim 5

A process according to claim 1 wherein the organic diisocyanate and the dicarboxylic acid are admixed in the molten state.

Claim 6

A process according to claim 1 wherein the dicarboxylic acid is selected from the group consisting of aromatic dicarboxylic acids, aliphatic dicarboxylic acids, carboxylic acid-terminated polyols and mixtures of any two or more such acids.

Claim 7

A process according to claim 1 wherein the heating of the initial mixture of reactants is carried out in a reaction zone from which evolved gases are readily vented.

Claim 8

A process according to claim 6 wherein said reaction zone comprises an open tray which is heated to a temperature such that the temperature of the reaction mixture lies within the range of about 100° C. to about 230° C.

Claim 9

A continuous process for the preparation, in the absence of an inert organic solvent, of a thermoplastic polymer which is characterized by a recurring amide linkage which process comprises the steps of: continuously feeding an organic diisocyanate and a dicarboxylic acid in the liquid state and in substantially stoichiometric proportions to a mixing zone at a temperature less than that at which any significant reaction occurs; mixing said reactants in said mixing zone and continuously passing said mixed reactants to a continuously moving endless conveyor belt; passing said mixed reactants on said moving conveyor belt through a heating zone maintained at a temperature in the range of about 100° C. to about 230° C. the residence time in said heating zone being adjusted so that between about 25 percent to about 95 percent of the theoretical amount of carbon dioxide necessary to achieve complete reaction has been evolved; continuously conveying the intermediate so produced to a comminution zone and subjecting the product to comminution; and completing the formation of the desired polymer by continuously melt extruding the comminuted material at a temperature above about 230° C. but below that at which degradation of the polymer occurs.

Claim 10

A continuous process for the preparation, in the absence of an inert organic solvent, of a thermoplastic polymer which is characterized by a recurring amide linkage which process comprises the steps of: continuously feeding an organic diisocyanate and a dicarboxylic acid in the liquid state and in substantially stoichiometric proportions to a mixing zone at a temperature less than that at which any significant reaction occurs; mixing said reactants in said mixing zone and continuously passing said mixed reactants to a continuously moving endless conveyor belt; passing said mixed reactants on said moving conveyor belt through a heating zone maintained at a temperature in the range of about 100° C. to about 230° C. the residence time in said heating zone being adjusted so that between about 25 percent to about 95 percent of the theoretical amount of carbon dioxide necessary to achieve complete reaction has been evolved; continuously conveying the intermediate so produced to a comminution zone and subjecting the product to comminution; and completing the formation of the desired polymer by continuously melt extruding the comminuted material at a temperature above about 230° C. but below that at which degradation of the polymer occurs.

Claim 11

A process according to claim 8 wherein the residence time in said heating zone is adjusted so that at least 50 percent of the theoretical amount of carbon dioxide has been evolved.

Claim 12

A process according to claim 8 wherein the dicarboxylic acid is selected from the group consisting of aromatic dicarboxylic acids, aliphatic dicarboxylic acids, carboxylic acid-terminated polyols and mixtures of any two or more of such acids.

Claim 13

A process according to claim 1 or 8 wherein the organic polyisocyanate is 4,4'-methylenebis(phenyl isocyanate) and the dicarboxylic acid is a mixture of adipic acid and azelaic acid.

Claim 14

A process according to claim 11 wherein the dicarboxylic acid component also comprises a dicarboxylic acid-terminated tetramethylene azelate.

Claim 15

A process according to claim 1 or 8 wherein the organic polyisocyanate is 4,4'-methylenebis(phenyl isocyanate) and the dicarboxylic acid is a mixture of azelaic acid and a dicarboxylic acid-terminated hexamethylene adipate.

Claim 16

A process according to claim 1 or 8 wherein the organic polyisocyanate is 4,4'-methylenebis(phenyl isocyanate) and the dicarboxylic acid component is a mixture of azelaic acid, adipic acid and a dicarboxylic acid terminated tetramethylene azelate.