Fibre containing polymers and process for production thereof

Claim 2

A process for the production of mixtures of polymer and fibrous material, said process comprising the steps of providing an agitated aqueous solution of coagulant for the polymer, said coagulant being selected from the group consisting of calcium chloride, sulfuric acid plus sodium chloride, sulphuric acid plus sodium chloride plus polyamine compound, alum, and alum plus sulphuric acid, adding an aqueous suspension of said fibrous material to the coagulant solution, adding said polymer in aqueous latex form to said coagulant solution and co-coagulating said polymer and fibrous material, and recovering and drying the mixture of polymer and fibrous material, said fibrous material being a polymeric paraphenylene terephthalamide aramid having an average length of from about 1 to about 5 mm and a BET surface area of greater than 1 m 2 /g.

Claim 3

The process of claim 1 wherein the fibrous material is the aramid fibre used in the wet pulp form and having a BET surface area of from about 7 to about 12 m 2 /g.

Claim 4

The process of claim 2 wherein the polymer in aqueous latex form is selected from synthetic rubbery polymers produced by emulsion polymerization and from other synthetic rubbery polymers in latex form.

Claim 5

The process of claim 3 wherein the polymer in aqueous latex form is selected from synthetic rubbery polymers produced by emulsion polymerization comprising styrene-butadiene polymers, butadiene-acrylonitrile polymers, carboxylated styrene-butadiene polymers, carboxylated butadiene-acrylonitrile polymers, polymers comprising chloroprene and polymers comprising acrylic monomers.

Claim 6

The process of claim 3 wherein the polymer in aqueous latex form is selected from other synthetic rubbery polymers in latex form comprising butyl rubber, halogenated butyl rubber, polybutadiene and ethylene-propylene-non-conjugated diene polymers.

Claim 7

The process of claim 2 wherein the amount of fibrous material in the mixture of polymer and fibrous material is from about 0.25 to about 20 parts by weight of fibrous material per 100 parts by weight of polymer.

Claim 8

The process of claim 2 wherein the amount of fibrous material in the mixture of polymer and fibrous material is from about 0.25 to about 100 parts by weight of fibrous material per 100 parts by weight of polymer.

Claim 9

The process of claim 2 wherein the aqueous latex contains from about 10 to about 45 weight percent of polymer based on the latex and the coagulation is undertaken with the coagulant solution maintained at a temperature of from about 25° to about 80° C.

Claim 10

The process of claim 2 wherein the co-coagulation is a continuous process in which the suspension of fibrous material is added continuously or intermittently to the coagulant solution while the latex is being added provided that part of the suspension of fibrous material is present in the coagulant solution before the addition of latex is initiated.

Claim 11

The process of claim 2 in which the polymer in aqueous latex form is selected from synthetic rubbery polymers produced by emulsion polymerization, the amount of fibrous material in the mixture of polymer and fibrous material is from about 0.25 to about 20 parts by weight per 100 parts by weight of polymer and the coagulation is undertaken with the coagulant solution maintained at a temperature of from about 25° to about 80° C.

Claim 12

The process of claim 10 wherein the polymer is selected from a styrene-butadiene polymer, an acrylonitrile-butadiene polymer and a polymer comprising chloroprene.

Claim 13

Polymer-fibrous material mixtures produced by the process of claim 1.

Claim 14

Polymer-fibrous material mixtures produced by the process of claim 10.

Claim 15

Polymer-fibrous material mixtures produced by the process of claim 11.

Claim 16

Vulcanizates produced by the steps comprising mixing a mixture of polymer and fibrous material with rubber compounding ingredients and vulcanization active agents, shaping the so-formed mixture and vulcanizing the shaped mixture by heating at an elevated temperature, wherein said mixture of polymer and fibrous material is produced by the process comprising the steps of providing an agitated aqueous solution of coagulant for the polymer, said coagulant being selected from the group consisting of calcium chloride, sulphuric acid plus sodium chloride, sulphuric acid plus sodium chloride plus polyamine compound, alum, and alum plus sulphuric acid, adding an aqueous suspension of said fibrous material to the coagulant solution, adding said polymer in aqueous latex form to said coagulant solution and co-coagulating said polymer and fibrous material, and recovering and drying the mixture of polymer and fibrous material, said fibrous material being a polymeric paraphenylene terephthalamide aramid having an average length of from about 1 to about 5 mm and a BET surface area of greater than 1 m 2 /g.

Claim 17

Vulcanizates produced by the steps comprising mixing a mixture of polymer and fibrous material with rubber compounding ingredients and vulcanization active agents, shaping the so-formed mixture and vulcanizing the shaped mixture by heating at an elevated temperature, wherein said mixture of polymer and fibrous material is produced by the process comprising the steps of providing an agitated aqueous solution of coagulant for the polymer, said coagulant being selected from the group consisting of calcium chloride, sulphuric acid plus sodium chloride, sulphuric acid plus sodium chloride plus polyamine compound, alum, and alum plus sulphuric acid, adding an aqueous suspension of said fibrous material to the coagulant solution, adding said polymer in aqueous latex form to said coagulant solution and co-coagulating said polymer and fibrous material, and recovering and drying the mixture of polymer and fibrous material, said fibrous material being a polymeric paraphenylene terephthalamide aramid having an average length of from about 1 to about 5 mm and a BET surface area of greater than 1 m 2 /g.

Claim 18

The vulcanizate of claim 15 wherein the polymer in aqueous form is selected from synthetic rubbery polymers produced by emulsion polymerization, the amount of fibrous material in the mixture of polymer and fibrous material is from about 0.25 to about 20 parts by weight per 100 parts by weight of polymer and the rubber compounding ingredients include any one or more of filler, extender or plasticizer, antioxidant and antiozonant.

Claim 19

The vulcanizate of claim 16 in which the polymer is selected from a styrene-butadiene polymer, an acrylonitrile-butadiene polymer and a polymer comprising chloroprene.

Claim 20

The vulcanizate of claim 15 wherein the shaped mixture is vulcanized by heating at a temperature of from about 140° to about 250° C. for a time of from about 5 to about 120 minutes.

Claim 21

The vulcanizate of claim 15 wherein the mixture of polymer and fibrous material is mixed with one or more compatible polymers.