Silicone rubber compositions for liquid injection molding machines

Claim 2

A silicone rubber composition which in the uncured state does not have a viscosity that exceeds 1.5×10 6 centipoise at 25° C. and has a Durometer in the cure state that exceeds 60 comprising: (A) 100 parts by weight of a linear vinyl terminated diorganopolysiloxane polymer having a viscosity that is in the range of 100 to 100,000 centipoise at 25° C. where the organo group is a monovalent hydrocarbon radical and the vinyl content varies from 0.05 to 0.20 weight percent; (B) from 10 to 50 parts by weight of fumed silica; (C) from 5 to 50 parts by weight of calcined diatomaceous earth; (D) from 1 to 200 parts per million of platinum as a platinum catalyst; and (E) from 1 to 50 parts by weight of a hydride-containing organopolysiloxane cross-linking agent wherein the hydrogen content varies from 0.2 to 1.0 percent by weight where the organo group is a monovalent hydrocarbon radical.

Claim 3

The composition of claim 1 wherein there is further present from 20 to 50 parts by weight of an organopolysiloxane copolymer comprising (R) 3 SiO 0 .5 units and SiO 2 units where R is a member selected from the class consisting of vinyl radicals and monovalent hydrocarbon radicals free of aliphatic unsaturation and where the ratio of monofunctional units to tetrafunctional units is from about 0.5 to 1 to 1 to 1 and where there is from about 0.002 to 10 mole percent of vinyl groups.

Claim 4

The composition of claim 1 wherein there is further present from 20 to 50 parts by weight of an organopolysiloxane copolymer comprising (R') 3 SiO 0 .5 units, SiO 2 units and R 2 'SiO units where R' is a group selected from the class consisting of vinyl radicals and monovalent hydrocarbon radicals free of aliphatic unsaturation where the ratio of (R') 3 SiO 0 .5 units to the SiO 2 units is between 0.5 to 1 to 1 to 1 and the (R') 2 SiO units are present in an amount equal to from about 1 to 10 mole percent based on the total number of mole percent of siloxane units in the copolymer and the vinyl concentration in the copolymer varies from 0.002 to 10.0 percent.

Claim 5

The composition of claim 2 wherein the fumed silica is treated with cyclopolysiloxanes prior to being incorporated in the composition.

Claim 6

The composition of claim 4 wherein the fumed silica is treated with silazanes and is present at a concentration of 10 to 25 parts by weight.

Claim 7

The composition of claim 5 wherein the diatomaceous earth is present at a concentration of 10 to 30 parts by weight.

Claim 8

The composition of claim 6 wherein the platinum catalyst is solubilized platinum complex.

Claim 9

The composition of claim 7 wherein the platinum catalyst is platinum complexed with an aliphatic alcohol.

Claim 10

The composition of claim 7 wherein the platinum catalyst is platinum complexed with a vinyl-containing cyclopolysiloxane.

Claim 11

The composition of claim 7 wherein the platinum catalyst is platinum complexed with a low molecular weight linear vinyl-terminated polysiloxane.

Claim 12

The composition of claim 8 wherein the hydride organopolysiloxane is a resinous copolymer having ##STR5## units and SiO 2 units where the H+R 2 to Si ratio varies from 1.0 to 2.7 where R 2 is a monovalent hydrocarbon radical free of aliphatic unsaturation.

Claim 13

The composition of claim 8 wherein the hydride organopolysiloxane is a resinous copolymer having ##STR6## units and SiO 2 and R 2 3 SiO units where the H+R 3 to Si ratio varies from 1.2 to 2.7 and where R 3 is a monovalent hydrocarbon radical free of aliphatic unsaturation.

Claim 14

The composition of claim 8 wherein the hydride organopolysiloxane is a linear copolymer having the formula ##STR7## where t is 0 or an integral number and s, t vary such that viscosity of the polymer varies from 10 to 1,000 centipoise at 25° C. and R 4 is a monovalent hydrocarbon radical free of aliphatic unsaturation.

Claim 15

The composition of claim 13 wherein the linear vinyl-terminated polysiloxane has the formula ##STR8## where Vi is vinyl, R 6 is a monovalent hydrocarbon radical and R 5 is a monovalent hydrocarbon radical free of aliphatic unsaturation and z varies such that the viscosity of the polymer varies from 100 to 100,000 centipoise at 25° C.

Claim 16

The composition of claim 14 wherein there is present at least 0.001 parts by weight of an inhibitor selected from the class consisting of acetylenic alcohols, hydroperoxide containing compounds, alkenyl-containing maleates, alkenyl isocyanurates and mixtures thereof.

Claim 17

A process for forming a silicione rubber composition which in the uncured state does not have a viscosity that exceeds 1.5×10 6 centipoise at 25° C. and has a Durometer in the cured state that exceeds 60 comprising: (1) mixing (A) 100 parts by weight of a linear vinyl terminated diorganopolysiloxane polymer having a viscosity that is in the range of 100 to 100,000 centipoise at 25° C. where the organo group is a monovalent hydrocarbon radical and the vinyl content varies from 0.05 to 0.20 weight percent; (B) from 10 to 50 parts by weight of fumed silica; (C) from 5 to 50 parts by weight of calcined diatomaceous earth; (D) from 1 to 200 parts per million of platinum as a platinum catalyst; and (E) from 1 to 50 parts by weight of a hydride organopolysiloxane cross-linking agent wherein the hydrogen content varies from 0.2 to 1.0 percent by weight where the organo group is a monovalent hydrocarbon radical; and (2) heating the composition so as to allow the composition to cure to a silicone elastomer.

Claim 18

A process for forming a silicione rubber composition which in the uncured state does not have a viscosity that exceeds 1.5×10 6 centipoise at 25° C. and has a Durometer in the cured state that exceeds 60 comprising: (1) mixing (A) 100 parts by weight of a linear vinyl terminated diorganopolysiloxane polymer having a viscosity that is in the range of 100 to 100,000 centipoise at 25° C. where the organo group is a monovalent hydrocarbon radical and the vinyl content varies from 0.05 to 0.20 weight percent; (B) from 10 to 50 parts by weight of fumed silica; (C) from 5 to 50 parts by weight of calcined diatomaceous earth; (D) from 1 to 200 parts per million of platinum as a platinum catalyst; and (E) from 1 to 50 parts by weight of a hydride organopolysiloxane cross-linking agent wherein the hydrogen content varies from 0.2 to 1.0 percent by weight where the organo group is a monovalent hydrocarbon radical; and (2) heating the composition so as to allow the composition to cure to a silicone elastomer.

Claim 19

The process of claim 16 where there is further present from 20 to 50 parts by weight of an organopolysiloxane copolymer comprising (R) 3 SiO 0 .5 units and SiO 2 units where R is a member selected from the class consisting of vinyl radicals and monovalent hydrocarbon radicals free of aliphatic unsaturation and where the ratio of monofunctional units to tetrafunctional units is from about 0.5 to 1 to 1 to 1 and where there is from about 0.002 to 10 mole percent of vinyl groups.

Claim 20

The process of claim 16 where there is further present from 20 to 50 parts by weight of an organopolysiloxane copolymer comprising (R') 3 SiO 0 .5 units, SiO 2 units, R 2 'SiO units, where R' is a group selected from the class consisting of vinyl radicals and monovalent hydrocarbon radicals free of aliphatic unsaturation where the ratio of (R') 3 SiO 0 .5 units to the SiO 2 units is between 0.5 to 1 to 1 to 1 and (R') 2 SiO units are present in an amount equal to from about 1 to 10 mole percent based on the total number of mole percent of siloxane units in the copolymer and the vinyl concentration in the copolymer varies from 0.002 to 10.0 mole percent.

Claim 21

The process of claim 17 wherein the fumed silica is treated with cyclopolysiloxane prior to being incorporated in the process.

Claim 22

The process of claim 19 wherein the fumed silica is treated with silazanes and is present at a concentration of 10 to 25 parts by weight.

Claim 23

The process of claim 20 wherein the diatomaceous earth is present in a concentration of 10-30 parts by weight.

Claim 24

The process of claim 21 wherein the platinum catalyst is a solubilized platinum catalyst.

Claim 25

The process of claim 22 wherein the platinum catalyst is platinum complexed with an aliphatic alcohol.

Claim 26

The process of claim 22 wherein the platinum catalyst is platinum complexed with a vinyl-containing cyclopolysiloxane.

Claim 27

The process of claim 22 wherein the platinum catalyst is platinum complexed with a low molecular weight linear vinyl-terminated polysiloxane.

Claim 28

The process of claim 23 wherein the hydride organopolysiloxane is a resinous copolymer having ##STR9## units and SiO 2 units where the H+R 2 to Si ratio varies from 1.0 to 2.7 where R 2 is a monovalent hydrocarbon radical free of aliphatic unsaturation.

Claim 29

The process of claim 23 wherein the hydride organopolysiloxane is a resinous copolymer having ##STR10## units and SiO 2 and R 2 3 SiO units where the H+R 3 to Si ratio varies from 1.2 to 2.7 and where R 3 is a monovalent hydrocarbon radical free of aliphatic unsaturation.

Claim 30

The process of claim 23 wherein the hydride organopolysiloxane is a linear copolymer having the formula ##STR11## where t is 0 or an integral number and s, t vary such that viscosity of the polymer varies from 10 to 1,000 centipoise at 25° C. and R 4 is a monovalent hydrocarbon radical free of aliphatic unsaturation.

Claim 31

The process of claim 28 wherein the linear vinyl-terminated polysiloxane has the formula ##STR12## where Vi is vinyl, R 6 is a monovalent hydrocarbon radical and R 5 is a monovalent hydrocarbon radical free of aliphatic unsaturation and z varies such that the viscosity of the polymer varies from 100 to 100,000 centipoise at 25° C.

Claim 32

The process of claim 29 wherein there is present at least 0.001 parts by weight of an inhibitor selected from the class consisting of acetylenic alcohols, hydroperoxide-containing compounds, alkenyl-containing maleates, alkenyl isocyanurates and mixtures thereof.

Claim 33

The process of claim 30 wherein the composition is formed into a part, in a liquid injection molding machine of the plunger type.

Claim 34

The process of claim 30 wherein the composition is heated to cure it to a silicone elastomer in a reciprocating screw type of liquid injection molding machine.

Claim 35

A process for forming a silicone elastomeric part which has a Durometer in the cure state that exceeds 60 and an Elongation that exceeds 200% and which in the silicone composition in the uncured state has a viscosity that does not exceed 1.5×10 6 centipoise at 25° C., comprising (1) passing into a liquid injection molding machine a silicone composition having: (A) 100 parts by weight of a linear vinyl terminated diorganopolysiloxane polymer having a viscosity that is in the range of 100 to 100,000 centipoise at 25° C. where the organo group is a monovalent hydrocarbon radical and the vinyl content varies from 0.05 to 0.20 weight percent: (B) from 10 to 50 parts by weight of fumed silica; (C) from 5 to 50 parts by weight of calcined diatomaceous earth; (D) from 1 to 200 parts per million of platinum as a platinum catalyst; and (E) from 1 to 50 parts by weight of a hydride organopolysiloxane cross-linking agent wherein the hydrogen content varies from 0.2 to 1.0 percent by weight where the organo group is a monovalent hydrocarbon radical; (2) heating the above composition in the liquid injection molding machine so as to form an elastomeric part; and (3) ejecting the formed part from the liquid injection molding machine.

Claim 36

A process for forming a silicone elastomeric part which has a Durometer in the cure state that exceeds 60 and an Elongation that exceeds 200% and which in the silicone composition in the uncured state has a viscosity that does not exceed 1.5×10 6 centipoise at 25° C., comprising (1) passing into a liquid injection molding machine a silicone composition having: (A) 100 parts by weight of a linear vinyl terminated diorganopolysiloxane polymer having a viscosity that is in the range of 100 to 100,000 centipoise at 25° C. where the organo group is a monovalent hydrocarbon radical and the vinyl content varies from 0.05 to 0.20 weight percent: (B) from 10 to 50 parts by weight of fumed silica; (C) from 5 to 50 parts by weight of calcined diatomaceous earth; (D) from 1 to 200 parts per million of platinum as a platinum catalyst; and (E) from 1 to 50 parts by weight of a hydride organopolysiloxane cross-linking agent wherein the hydrogen content varies from 0.2 to 1.0 percent by weight where the organo group is a monovalent hydrocarbon radical; (2) heating the above composition in the liquid injection molding machine so as to form an elastomeric part; and (3) ejecting the formed part from the liquid injection molding machine.

Claim 37

The process of claim 33 wherein the liquid injection molding machine is a plunger type of liquid injection molding machine.

Claim 38

The process of claim 33 wherein the liquid injection molding machine is a reciprocating screw type of liquid injection molding machine.

Claim 39

The process of claim 35 wherein there is further present from 20 to 50 parts by weight of an organopolysiloxane copolymer comprising (R) 3 SiO 0 .5 units and SiO 2 units where R is a member selected from the class consisting of vinyl radicals and monovalent hydrocarbon radicals free of aliphatic unsaturation and where the ratio of monofunctional units to tetrafunctional units is from about 0.5 to 1 to 1 to 1 and where there is from about 0.002 to 10 mole percent of vinyl groups.

Claim 40

The process of claim 35 wherein in the silicone composition there is further present from 20 to 50 parts by weight of an organopolysiloxane copolymer comprising (R') 3 SiO 0 .5 units, SiO 2 units, and R 2 'SiO units where R' is a group selected from the class consisting of vinyl radicals free of aliphatic unsaturation where the ratio of (R') 2 SiO units are present in an amount equal to from about 1 to 10 mole percent based on the total number of moles of siloxane units in the copolymer and the vinyl concentration in the copolymer varies from 0.002 to 10.0 mole percent.

Claim 41

The process of claim 36 wherein the fumed silica is treated with cyclopolysiloxanes prior to being incorporated in the composition.

Claim 42

The process of claim 38 wherein the fumed silica is treated with silazanes and is present at a concentration of 10 to 25 parts by weight.

Claim 43

The process of claim 39 wherein the diatomaceous earth is present in a concentration of 10 to 30 parts by weight.

Claim 44

The process of claim 40 wherein the platinum catalyst is a solubilized platinum complex.

Claim 45

The process of claim 41 wherein the platinum catalyst is platinum complexed with an aliphatic alcohol.

Claim 46

The process of claim 41 wherein the platinum catalyst is platinum complexed with a vinyl-containing cyclopolysiloxane.

Claim 47

The process of claim 41 wherein the platinum catalyst is platinum complexed with a low molecular weight linear vinyl-terminated polysiloxane

Claim 48

The process of claim 42 wherein the hydride organopolysiloxane is a resinous copolymer having ##STR13## units and SiO 2 units where the H+R 2 to Si ratio varies from 1.0 to 2.7 where R 2 is a monovalent hydrocarbon radical free of aliphatic unsaturation.

Claim 49

The process of claim 42 wherein the hydride organopolysiloxane is a resinous copolymer having the formula ##STR14## units and SiO 2 and R 2 3 SiO units where the H+R 3 to Si ratio varies from 1.2 to 2.7 and where R 3 is a monovalent hydrocarbon radical free of aliphatic unsaturation.

Claim 50

The process of claim 42 wherein the hydride organopolysiloxane is a linear copolymer having the formula ##STR15## where t is 0 or an integral number and s, t vary such that viscosity of the polymer varies from 10 to 1,000 centipoise at 25° C. and R 4 is a monovalent hydrocarbon radical free of aliphatic unsaturation.

Claim 51

The process of claim 47 wherein the linear vinyl-terminated polysiloxane has the formula ##STR16## where Vi is vinyl, R 6 is a monovalent hydrocarbon radical and R 5 is a monovalent hydrocarbon radical free of aliphatic unsaturation and z varies such that the viscosity of the polymer varies from 100 to 100,000 centipoises at 25° C.

Claim 52

The process of claim 48 wherein there is present at least 0.001 parts by weight of an inhibitor selected from the class consisting of acetylenic alcohols, hydroperoxide containing compounds, alkenyl-containing maleates, alkenyl isocyanurates and mixtures thereof.