초록 ▼

The present invention relates to a process for improving the cured adhesion of at least two rubber components which contact each other in a pneumatic tire. The process involves the steps of assembling and vulcanizing a pneumatic tire wherein prior to vulcanization of the pneumatic tire, one of the c

The present invention relates to a process for improving the cured adhesion of at least two rubber components which contact each other in a pneumatic tire. The process involves the steps of assembling and vulcanizing a pneumatic tire wherein prior to vulcanization of the pneumatic tire, one of the components is a precured rubber compound and the other is an uncured rubber compound. The process involves using a precured rubber compound comprising from 40 to 100 parts by weight of natural rubber or emulsion-polymerized styrene-butadiene copolymer rubber containing 0.5 to 3 phr of a fatty acid, precipitated silica and no fatty acid other than contained in the natural rubber or emulsion-polymerized styrene-butadiene rubber.

대표청구항 ▼

1. A process for improving the cured adhesion of a precured rubber component in a pneumatic tire to an uncured rubber component in a tire comprising (A) assembling the tire so a precured rubber component is in contact with an uncured rubber component wherein said precured rubber component compris

1. A process for improving the cured adhesion of a precured rubber component in a pneumatic tire to an uncured rubber component in a tire comprising (A) assembling the tire so a precured rubber component is in contact with an uncured rubber component wherein said precured rubber component comprises (1) from 40 to 100 parts by weight of a rubber, per 100 parts by weight of total rubber in said precured rubber compound, selected from the group consisting of natural rubber, emulsion-polymerized styrene-butadiene rubber and mixtures thereof, wherein said rubber contains from 0.5 to 3 phr of a fatty acid inherently present in the natural rubber or present from the polymerization reaction to produce the styrene-butadiene rubber; (2) from 3 to 80 phr of precipitated silica; (3) from 0.8 to 3.5 phr of an accelerator; (4) from 1.0 to 3.5 phr of sulfur, wherein the weight ratio of accelerator to sulfur ranges from 0.5:1 to 3.5:1; (5) from 1 to 10 phr of zinc oxide; and (6) 0 phr of any fatty acid other than the 0.5 to 3 phr present in said natural rubber and emulsion-polymerized styrene-butadiene rubber; and (B) vulcanizing the tire at a temperature ranging from 120° C. to 200° C. 2. The process of claim 1 wherein from 50 to 100 parts by weight of said rubber is selected from the group consisting of natural rubber, emulsion-polymerized styrene-butadiene rubber and mixtures thereof. 3. The process of claim 1 wherein said components are selected from the group consisting of a tread, apex and innerliner. 4. The process of claim 3 wherein said precured rubber component is selected from the group consisting of a tread, apex and innerliner. 5. The process of claim 1 wherein from 5 to 20 phr of silica is present. 6. The process of claim 1 wherein said accelerator is selected from the group consisting of amines, disulfides, guanidines, thioureas, thiazoles, thiurams, sulfenamides, dithiocarbamates, xanthates and mixtures thereof. 7. The process of claim 1 wherein said rubber in said precured rubber composition is natural rubber. 8. The process of claim 1 wherein said rubber in said precured rubber composition is emulsion-polymerized styrene-butadiene rubber. 9. The process of claim 1 wherein from 0 to 60 parts by weight of said rubber in said precured rubber compound is selected from the group consisting of solution polymerized stryene/butadiene copolymers, cis 1,4-polybutadiene, synthetic cis 1,4-polyisoprene, styrene/isoprene copolymers, 3,4-polyisoprene, isoprene/butadiene copolymers, medium vinyl polybutadiene, styrene/isoprene/butadiene terpolymers, butyl rubber, polychloroprene, acrylonitrile/butadiene copolymers and ethylene/propylene/diene terpolymers and mixtures thereof. 10. The process of claim 1 wherein the weight ratio of accelerator to sulfur ranges from about 0.5:1 to 2:1. 11. The process of claim 1 wherein said rubber is natural rubber and the concentration range of said precipitated silica is from 5 to 15 phr.