Process for the continuous manufacture of silicone gums

Claim 2

A process for the continuous polymerization of polydiorganosiloxanes comprising: (a) mixing one or more cyclopolysiloxane monomers with one or more chainstopping agents, (b) preheating the mixture resulting from (a), (c) adding to the preheated mixture of (b) an amount of catalyst effective for catalyzing a polymerization reaction, (d) polymerizing the catalyzed mixture of (c) in a screw extruder having essentially plug flow therethrough, and (e) adding to the resulting polydiorganosiloxane an amount of neutralizing agent effective for neutralizing said catalyst.

Claim 3

A process for the continuous polymerization of polydiorganosiloxane comprising: (a) mixing one or more cyclopolysiloxane monomers with one or more chainstopping agents, (b) preheating the mixture resulting from (a), (c) adding to the preheated mixture of (b) an amount of catalyst effective for catalyzing a polymerization reaction, (d) partially polymerizing the catalyzed mixture of (c) in a static mixer and/or a scraped surface reactor having essentially plug flow therethrough, (e) passing the partially polymerized mixture of (d) to a screw extruder having essentially plug flow therethrough and completing the polymerization reaction therein, and (f) adding to the resulting polydiorganosiloxane an amount of neutralizing agent effective for neutralizing said catalyst.

Claim 4

A process for the continuous polymerization of polydiorganosiloxane comprising: (a) mixing one or more cyclopolysiloxane monomers with one or more chainstopping agents, (b) preheating the mixture resulting from (a), (c) adding to the preheated mixture of (b) an amount of catalyst effective for catalyzing a polymerization reaction, (d) partially polymerizing the catalyzed mixture of (c) in a static mixer and/or a scraped surface reactor having essentially plug flow therethrough, (e) passing the partially polymerized mixture of (d) to a screw extruder having essentially plug flow therethrough and completing the polymerization reaction therein, and (f) adding to the resulting polydiorganosiloxane an amount of neutralizing agent effective for neutralizing said catalyst.

Claim 5

A process as set forth in claims 1 or 2 wherein after mixing one or more cyclopolysiloxane monomers with one or more chainstopping agents, the resulting mixture is passed through a drying means.

Claim 6

A process as set forth in claim 3 wherein said drying means is a molecular sieve.

Claim 7

A process as set forth in claim 3 wherein after the mixture of one or more cyclopolysiloxanes and one or more chainstopping agents is passed through a drying means, said mixture is preheated and degassed.

Claim 8

A process as set forth in claim 2 wherein the partial polymerization of step (d) is effected at a temperature within the range of from about 130° C. to about 200° C.

Claim 9

A process as set forth in claim 2 wherein the partial polymerization of step (d) is effected at a temperature within the range of from about 140° C. to about 180° C.

Claim 10

A process as set forth in claim 1 or 2 wherein the cyclopolysiloxane monomer has the formula ##STR5## wherein n is an integer from 3 to 8 and R is a substituted or unsubstituted hydrocarbon radical.

Claim 11

A process as set forth in claim 8 wherein n is an integer equal to 3, 4 or 5 an R is an unsubstituted hydrocarbon radical.

Claim 12

A process as set forth in claim 8 wherein n equals 4 and R is methyl.

Claim 13

A process as set forth in claims 1 or 2 wherein the chainstopping agent is selected from the group consisting of trialkylsiloxy chainstopper, dialkylvinylsiloxy chainstopper and silanol chainstopper.

Claim 14

A process as set forth in claims 1 or 2 wherein the preheating of step (b) results in the mixture of cyclopolysiloxanes and chainstopping agents from step (a) having a temperature in the range of from about 150° C. to about 175° C.

Claim 15

A process as set forth in claims 1 or 2 wherein the catalyst is potassium silanolate and the neutralizing agent is silyl phosphate.

Claim 16

A process as set forth in claims 1 or 2 wherein the resulting polydiorganosiloxane has a viscosity of at least 500,000 centipoise when measured at 25° C.

Claim 17

A process as set forth in claims 1 or 2 wherein the resulting polydiorganosloxane has a viscosity of at least 1,000,000 centipoise when measured at 25° C.

Claim 18

A process as set forth in claims 1 or 2 wherein the resulting polydiorganosiloxane has a viscosity ranging from about 2,000,000 to about 150,000,000 centipoise when measured at 25° C.

Claim 19

A process as set forth in claims 1 or 2 wherein the screw extruder having essentially plug flow therethrough is a single screw extruder.

Claim 20

A process as set forth in claim 17 wherein said single screw extruder also provides kneading.

Claim 21

A process as set forth in claims 1 or 2 wherein the screw extruder having essentially plug flow therethrough is operated at a temperature within the range of from about 130° C. to about 250° C.

Claim 22

A process as set forth in claims 1 or 2 wherein the screw extruder having essentially plug flow therethrough is operated at a temperature within the range of from about 175° C. to about 225° C.

Claim 23

A process as set forth in claims 1 or 2 wherein after neutralization of the catalyst contained in the resulting polydiorganosiloxane, said polydiorganosiloxane is substantially devolatilized.

Claim 24

A process as set forth in claim 21 wherein cyclopolysiloxanes removed by said devolatilization step are recycled for mixing with newly introduced cyclopolysiloxane monomer and chainstopping agent.

Claim 25

A process for the continuous polymerization of polydiorganosiloxane gums having a viscosity of from 2,000,000 to 150,000,000 centipoise at 25° C., comprising the steps: (a) mixing octamethylcyclotetrasiloxane with a chainstopping agent selected from the group consisting of trialkylsiloxy chainstopper, dialkylvinylsiloxy chainstopper and silanol chainstopper, (b) preheating the mixture resulting from step (a) to a temperature ranging from about 150° C. to about 175° C., (c) adding to the preheated mixture of step (b) an amount of potassium silanolate catalyst effective for catalyzing a polymerization reaction, (d) partially polymerizing the catalyzed mixture resulting from step (c) in a static mixer and/or a scraped surface reactor having essentially plug flow therethrough at a temperature in the range of from about 140° C. to about 180° C., (e) passing the partially polymerized mixture resulting from step (d) to a single screw extruder having kneading action and essentially plug flow therethrough, and completing the polymerization reaction therein at a temperature ranging from about 175° C. to about 225° C., (f) adding to the resulting polydiorganosiloxane having a viscosity ranging from 2,000,000 to 150,000,000 centipoise at 25° C., an amount of silyl phosphate effective for neutralizing said potassium silanolate catalyst, (g) substantially devolatilizing the polydiorganosiloxane resulting from step (f), and (h) recycling cyclopolysiloxanes obtained in step (g) for mixing with newly introduced cyclopolysiloxane monomer and chainstopping agent.

Claim 26

A process for the continuous polymerization of polydiorganosiloxane gums having a viscosity of from 2,000,000 to 150,000,000 centipoise at 25° C., comprising the steps: (a) mixing octamethylcyclotetrasiloxane with a chainstopping agent selected from the group consisting of trialkylsiloxy chainstopper, dialkylvinylsiloxy chainstopper and silanol chainstopper, (b) preheating the mixture resulting from step (a) to a temperature ranging from about 150° C. to about 175° C., (c) adding to the preheated mixture of step (b) an amount of potassium silanolate catalyst effective for catalyzing a polymerization reaction, (d) partially polymerizing the catalyzed mixture resulting from step (c) in a static mixer and/or a scraped surface reactor having essentially plug flow therethrough at a temperature in the range of from about 140° C. to about 180° C., (e) passing the partially polymerized mixture resulting from step (d) to a single screw extruder having kneading action and essentially plug flow therethrough, and completing the polymerization reaction therein at a temperature ranging from about 175° C. to about 225° C., (f) adding to the resulting polydiorganosiloxane having a viscosity ranging from 2,000,000 to 150,000,000 centipoise at 25° C., an amount of silyl phosphate effective for neutralizing said potassium silanolate catalyst, (g) substantially devolatilizing the polydiorganosiloxane resulting from step (f), and (h) recycling cyclopolysiloxanes obtained in step (g) for mixing with newly introduced cyclopolysiloxane monomer and chainstopping agent.

Claim 27

A process as set forth in claim 23 wherein after mixing said octamethylcyclotetrasiloxane and said chainstopping agent, the resulting mixture is passed through a drying means.

Claim 28

A process as set forth in claim 24 wherein after said mixture of octamethylcyclotetrasiloxane and chainstopping agent is dried, said mixture is preheated and degassed.