Compositions based on alkylene-alkyl acrylate copolymers and silanol condensation catalysts; and the use thereof in the production of covered wires and cables

Claim 2

A process of extruding a composition about a wire or cable which comprises soaking a composition consisting essentially of an alkylene-alkyl acrylate copolymer and a silanol codensation catalyst with an organo titanate, admixing said soaked composition with a polysiloxane or monomeric silane with the result that the polysiloxane or monomeric silane reacts with said alkylene-alkyl acrylate copolymer to produce a product containing a water-curable, silane modified alkylene-alkyl acrylate copolymer and extruding said product about a wire or cable.

Claim 3

A process as defined in claim 1 wherein said polysiloxane contains units of the formula: ##STR6## wherein R is a hydrocarbon radical or an oxy substituted hydrocarbon radical, each V is hydrogen, a hydrocarbon radical or a hydrolyzable group, Z is a hydrolyzable group, n is an integer having a value of one to 18 and x is an integer having a value of at least 2.

Claim 4

A process as defined in claim 1 wherein the monomeric silane has the formula: ##STR7## wherein R 1 is a hydrocarbon radical and the other variables are as defined in claim 2.

Claim 5

A process of extruding a composition about a wire or cable which comprises drying a composition consisting essentially of an alkylene-alkyl acrylate copolymer and a silanol condensation catalyst to a water content below about 500 ppm, soaking said dried composition with an organo titanate, admixing said soaked composition with a polysiloxane or monomeric silane with the result that the polysiloxane or monomeric silane reacts with said alkylene-alkyl acrylate copolymer to produce a product containing a water-curable, silane modified alkylenealkyl acrylate copolymer and extruding said product about a wire or cable.

Claim 6

A process of extruding a composition about a wire or cable which comprises drying a composition consisting essentially of an alkylene-alkyl acrylate copolymer and a silanol condensation catalyst to a water content below about 500 ppm, soaking said dried composition with an organo titanate, admixing said soaked composition with a polysiloxane or monomeric silane with the result that the polysiloxane or monomeric silane reacts with said alkylene-alkyl acrylate copolymer to produce a product containing a water-curable, silane modified alkylenealkyl acrylate copolymer and extruding said product about a wire or cable.

Claim 7

A process as defined in claim 4 wherein the silanol condensation catalyst is dibutyltin dilaurate, the copolymer is an ethylene-ethyl acrylate copolymer, the organo titanate is tetraisopropyl titanate and the polysiloxane has the formula: ##STR8##

Claim 8

A process of extruding a composition about a wire or cable which comprises soaking a composition consisting essentially of an alkylene-alkyl acrylate copolymer and a silanol condensation catalyst with an organo titanate, admixing said soaked composition with a polysiloxane or monomeric silane, conveying the resultant composition through a feed zone of an extruder, maintained at a temperature of about 100° C. to about 180° C. with the result that a substantially steady supply of said composition is fed from said feed zone to the next succeeding zone of the extruder, the transition zone, compressing said composition in said transition zone, while the temperature of said transition zone is maintained at about 130° C. to about 200° C., to melt said composition, feeding said melt to the next succeeding zone of the extruder, the metering zone, which is maintained at a temperature of about 130° C. to about 220° C., pressurizing said melt in said metering zone in order to convey said melt to the next succeeding zone of the extruder, the reaction zone, through the reaction zone and to the extrusion die orifice in a steady and metered out-put rate, from whence the reacted composition is extruded as a shaped product, the temperature of the reaction zone being maintained at about 130° C. to about 220° C. and the residence time of said composition within said reaction zone being sufficient to insure that a substantially complete reaction has occurred to form a water-curable, silane modified copolymer.

Claim 9

A process of extruding a composition about a wire or cable which comprises soaking a composition consisting essentially of an alkylene-alkyl acrylate copolymer and a silanol condensation catalyst with an organo titanate, admixing said soaked composition with a polysiloxane or monomeric silane, conveying the resultant composition through a feed zone of an extruder, maintained at a temperature of about 100° C. to about 180° C. with the result that a substantially steady supply of said composition is fed from said feed zone to the next succeeding zone of the extruder, the transition zone, compressing said composition in said transition zone, while the temperature of said transition zone is maintained at about 130° C. to about 200° C., to melt said composition, feeding said melt to the next succeeding zone of the extruder, the metering zone, which is maintained at a temperature of about 130° C. to about 220° C., pressurizing said melt in said metering zone in order to convey said melt to the next succeeding zone of the extruder, the reaction zone, through the reaction zone and to the extrusion die orifice in a steady and metered out-put rate, from whence the reacted composition is extruded as a shaped product, the temperature of the reaction zone being maintained at about 130° C. to about 220° C. and the residence time of said composition within said reaction zone being sufficient to insure that a substantially complete reaction has occurred to form a water-curable, silane modified copolymer.

Claim 10

A process as defined in claim 6 wherein the temperatures of said zones of the extruder are as follows: Feed zone--about 140° C. to about 160° C. Transition zone--about 150° C. to about 175° C. Metering zone--about 160° C. to about 190° C. Reaction zone--about 160° C. to about 190° C.

Claim 11

A process as defined in claim 6 wherein the organo titanate is tetraisopropyl titanate, the silane reactant is a polysiloxane, the alkylene-alkyl acrylate copolymer is an ethylene-ethyl acrylate copolymer and the silanol condensation catalyst is dibutyl tin dilaurate.

Claim 12

A process as defined in claim 6 wherein said resultant composition comprises a silanol condensation catalyst, tetraisopropyl titanate, a polysiloxane and an ethylene-ethyl acrylate copolymer.

Claim 13

A process as defined in claim 1 wherein the silanol condensation catalyst is dibutyl tin dilaurate.

Claim 14

A process as defined in claim 6 wherein the silanol condensation catalyst is dibutyl tin dilaurate.

Claim 15

A process as defined in claim 4 wherein the said water content is below about 300 ppm.