Foams prepared from polypropylene resin composition and process for producing same

Claim 2

A foam of polypropylene resin composition prepared from a composition comprising a mixture of (1) polypropylene resin and (2) 5-50 parts by weight per 100 parts by weight of the polypropylene resin of 1,2-polybutadiene resin which contains at least 70% of vinyl structure (1,2-bonds) and has an intrinsic viscosity (η) of at least 0.7 dl/g measured in toluene at 30° C. and a melting point of not lower than 40° C.; the foam being characterized in that it contains hot xylene insoluble thermal reaction products of 1,2-polybutadiene of at least 2% by weight based on the whole composition, and a hot xylene soluble content of 1,2-polybutadiene of up to 30% by weight based on the whole composition.

Claim 3

A foam as defined in claim 1 wherein the 1,2-polybutadiene is used in an amount of 10-30 parts by weight of the polypropylene resin.

Claim 4

A foam as defined in claim 1 wherein the polypropylene resin is isotactic homo-polypropylene resin.

Claim 5

A foam as defined in claim 1 wherein the polypropylene resin is stereospecific propylene-ethylene random copolymer.

Claim 6

A foam as defined in claim 1 wherein the polypropylene resin is stereospecific propylene-etylene block copolymer.

Claim 7

A foam as defined in claim 1 wherein the MI (as measured according to ASTM D-1238) of the propylene resin is up to 2.0.

Claim 8

A foam as defined in claim 1 which is in the form of a thick rectangular plate.

Claim 9

A foam as defined in claim 1 which is in the shape of a round bar.

Claim 10

A foam as defined in claim 1 which is prepared by an extrusion foaming process.

Claim 11

A foam as defined in claim 1 wherein a foaming degree is 10-50 times.

Claim 12

A process for preparing a foam from a polypropylene resin composition by melting and kneading a composition comprising polypropylene resin and a blowing agent at a high temperature suitable for foaming and thereafter extruding the cooled composition into a low pressure zone to obtain a foam of polypropylene resin, the process being characterized in that the composition incorporates 1,2-polybutadiene resin containing at least 70% of vinyl structure and having an intrinsic viscosity (η) of at least dl/g as measured in toluene at 30° C. and a melting point of at least 40° C., and that the composition is melted and kneaded at an elevated temperature at which the 1,2-polybutadiene resin, when partly or wholly subjected to thermal reaction, gives hot xylene insolubles in an amount of at least 2% by weight based on the whole composition, and the incorporated 1,2-polybutadiene resin has a hot xylene soluble content of up to 30% by weight based on the whole composition.

Claim 13

A process for preparing a foam from a polypropylene resin composition by melting and kneading a composition comprising polypropylene resin and a blowing agent at a high temperature suitable for foaming and thereafter extruding the cooled composition into a low pressure zone to obtain a foam of polypropylene resin, the process being characterized in that the composition incorporates 1,2-polybutadiene resin containing at least 70% of vinyl structure and having an intrinsic viscosity (η) of at least dl/g as measured in toluene at 30° C. and a melting point of at least 40° C., and that the composition is melted and kneaded at an elevated temperature at which the 1,2-polybutadiene resin, when partly or wholly subjected to thermal reaction, gives hot xylene insolubles in an amount of at least 2% by weight based on the whole composition, and the incorporated 1,2-polybutadiene resin has a hot xylene soluble content of up to 30% by weight based on the whole composition.

Claim 14

A process as defined in claim 11 wherein organic volatile blowing agents boiling at -40° C. to 60° C. at atmospheric pressure are used singly, or at least two of them are used in admixture.

Claim 15

A process as defined in claim 11 wherein the low pressure zone is at atmospheric pressure.

Claim 16

A process as defined in claim 11 wherein a cell nucleus forming agent is employed.

Claim 17

A process as defined in claim 14 wherein the cell nucleus forming agent is a member selected from the group consisting of talc, zinc white, calcium carbonate, sodium dicarbonate, citric acid, and metal salts of stearic acid.

Claim 18

A process as defined in claim 11 wherein the kneading temperature is in the range of 200° to 280° C.

Claim 19

A process as defined in claim 11 wherein at least one other thermoplastic resin is added to the composition comprising polypropylene resin and 1,2-polybutadiene resin.

Claim 20

A process as defined in claim 17 wherein the other thermoplastic resin is aromatic vinyl polymer.

Claim 21

A process as defined in claim 17 wherein the other thermoplastic resin is ethylene-α-olefin copolymer.