Compatible blends of thermoplastic molding compositions

1. A compatible blend composition comprising 99.99 to 90% by weight, relative to the entire blend, of at least two different incompatible thermoplastic molding compositions, 0.01 to 10% by weight, relative to the entire blend of carbodiimides and/or polycarbodiimides of the formula (I)

R′—(—N═C═N—R—) n —R″  (I),

where

R represents an aromatic radical wherein at least one ortho-position with respect to the aromatic carbon atom having the carbodiimide group, carries aliphatic and/or cycloaliphatic substituents with at least 2 C-atoms,

R′ represents aryl, aralkyl or R—NCO, R—NHCONHR 1 , R—NHCONR 1 R 2 or R—NHCOOR 3 ,

R″ represents —N═C═N-aryl, —N═C═N-aralkyl, —NCO, —NHCONHR 1 , —NHCONR 1 R 2 or —NHCOOR 3 ,

R 1 and R 2 are the same or different and represent an alkyl, cycloalkyl or aralkyl radical, and R 3 has one of the meanings of R 1 or represents a polyester or a polyamide radical, and

n represents an integer from 2 to 5,000; and

wherein

at least one of the thermoplastic molding compositions comprises at least one functional group selected from the group consisting of carboxylic acid, hydroxyl group, amino group, and mercaptan group, and

at least one of the thermoplastic molding compositions is a polyamide, and

at least one of the thermoplastic molding compositions is a thermoplastics polyester, said polyester consisting of one or more polyalkylene terephthalates wherein said thermoplastics polyester is neither derived from the reaction of one or more dihydric phenols with one or more aromatic dicarboxylic acids nor from 1,4-cyclohexanedimethanol.

2. A molded article comprising the composition according to claim 1 .

3. The molded articles according to claim 2 , wherein the article is a film(s) or fiber(s).

4. The molded articles according to claim 2 , wherein the article is a machine housing or motor vehicle part.

5. A method for producing a compatible blend composition comprising 99.99 to 90% by weight, relative to the entire blend, of at least two different incompatible thermoplastic molding compositions, comprising:

mixing

0.01 to 10% by weight, relative to the entire blend, of a carbodiimide(s) and/or polycarbodiimide(s) of the formula (I)

R′—(—N═C═N—R—) n —R′  (I),

where

R represents an aromatic radical wherein at least one ortho-position with respect to the aromatic carbon atom having the carbodiimides group, carries aliphatic and/or cycloaliphatic substituents with at least 2 C-atoms,

R′ represents aryl, aralkyl or R—NCO, R—NHCONHR 1 , R—NHCONR 1 R 2 or R—NHCOOR3,

R″ represents —N═C═N-aryl, —N═C═N-aralkyl, —NCO, —NHCONHR 1 , —NHCONR 1 R 2 or —NHCOOR 3 ,

R 1 and R 2 are the same or different and represent an alkyl, cycloalkyl or aralkyl radical, and R 3 has one of the meanings of R 1 or represents a polyester or a polyamide radical, and

n represents an integer from 2 to 5,000, with

at least two Thermoplastic molding compositions containing at least one functional group selected from the group consisting of carboxylic acid, hydroxyl group, amino group, and mercaptan group in a mixing unit above the melt temperature of at least one of the components,

wherein at least one of the thermoplastic molding compositions is a polyamide and wherein at least one of the thermoplastic molding compositions is a thermoplastic polyester, said polyester consisting of one or more polyalkylene terephthalates or mixtures thereof, wherein the thermoplastic polyester Is neither derived from the reaction of one or more dihydric phenols with one or more aromatic dicarboxylic acid nor from 1,4-cyclohexanedimethanol.

6. The method according to claim 5 , wherein the mixing unit is selected from the group of units consisting of kneaders, single-screw extruders, twin-screw extruders, cascade extruders, devolatilizing extruders, multi-screw extruders and planetary-gear extruders.

7. The method according to claim 6 , wherein the mixing unit is a closely intermeshing twin-screw extruder.

8. The method according to claim 6 , wherein the mixing unit is a single-screw extruder, which operates according to the stator/rotor principle.

9. The method according to claim 6 , wherein the mixing unit is a triple-screw extruder.

10. The method according to claim 6 , wherein the mixing unit is a multi-screw extruder which operates according to the planetary extruder principle.

11. The method according to claim 6 , wherein the mixing unit is a continuously or discontinuously operating co-kneader.

12. The method according to claim 6 , wherein the mixing unit is a continuously operating dispersion kneader with slow-speed rotor-stator combination.