Process for the continuous manufacture of siloxane polymers

Claim 2

A process for the continuous polymerization of silanol terminated diorganopolysiloxane polymers having a viscosity varying from 500 to 500,000 centipoise at 25° C. comprising: (a) mixing degassed and preheated cyclopolysiloxanes with an amount of a basic catalyst effective for catalyzing said continuous polymerization; (b) passing the mixture of the polysiloxane and catalyst into a mixer having static elements which provide essentially uniform plug flow characteristics to the catalyzed mixture passing therethrough, maintained under pressure and providing sufficient residence time for completion of the polymerization and controlling the polymer viscosity by introducing to the initial part of the static mixer reaction zone from 100 to 500 parts per million of water as a chain-stopper; (c) mixing into the reaction mixer an amount of a neutralizing agent effective for neutralizing the basic catalyst; and (d) passing the solution of the neutralizing agent and reaction mixture through a mixer for completion of the neutralization.

Claim 3

A process as in claim 1, further comprising the step of adding up to approximately 2500 ppm additional water chain-stopper near the terminal end of the static mixer reaction zone to further control polymer viscosity.

Claim 4

A process as in claim 1, wherein the basic catalyst is selected from the group consisting of cesium hydroxide, potassium hydroxide, sodium hydroxide, cesium silanolate, potassium silanolate and sodium silanolate.

Claim 5

A process as in claim 3, wherein the basic catalyst is potassium silanolate.

Claim 6

A process as in claim 1, wherein the static mixer reaction zone is maintained at a pressure slightly greater than the vapor pressure of water at the reaction zone temperature.

Claim 7

A process as in claim 5, wherein the reaction zone pressure is at least 170 psig.

Claim 8

A process as in claim 1, wherein the static mixer reaction zone temperature is approximately 160° C. to approximately 200° C.

Claim 9

A process as in claim 7, wherein the preferred temperature is from approximately 180° C. to approximately 190° C.

Claim 10

A process as in claim 1, wherein the residence time of the hot catalyzed monomer within the static mixer reaction zone is sufficient to provide less than approximately 16% unreacted monomer after the polymerization reaction.

Claim 11

A process as in claim 1, wherein the neutralizing agents are silyl phosphite and trischloroethyl phosphiate.

Claim 12

A process as in claim 10, wherein the neutralizing agent is silyl phosphate.

Claim 13

A process as in claim 1, wherein one mole equivalent of neutralizing acid is added for each mole equivalent of catalytic base utilized in the polymerization reaction.

Claim 14

A process as in claim 1, wherein the neutralization reaction takes place in a static mixer providing sufficient residence time for completion of the neutralization reaction.

Claim 15

The process for the continuous polymerization of triorganosilyldiorganopolysiloxane polymers having a viscosity varying from 10 to 1,000,000 centipoise at 25° C. comprising: (a) mixing dried degassed an preheated cyclopolysiloxanes with an amount of a basic catalyst effective for catalyzing said continuous polymerization; (b) passing the mixture of the polysiloxane and catalyst into a mixer having static elements which provide essentially uniform plug flow characteristics to the catalyzed mixture passing therethrough, maintained under pressure and providing sufficient residence time for completion of the polymerization, and controlling the polymer viscosity by introducing to the initial part of the static mixer reaction zone a low molecular weight triorganosilyldiorganopolysiloxane as a chain-stopper, and where the organo group is a monovalent hydrogen radical; (c) mixing into the reaction mixture an amount of a neutralizing agent effective to neutralize the basic catalyst and (d) passing the solution of the neutralizing agent and reaction mixture through a static mixer for completion of the neutralization.

Claim 16

The process for the continuous polymerization of triorganosilyldiorganopolysiloxane polymers having a viscosity varying from 10 to 1,000,000 centipoise at 25° C. comprising: (a) mixing dried degassed an preheated cyclopolysiloxanes with an amount of a basic catalyst effective for catalyzing said continuous polymerization; (b) passing the mixture of the polysiloxane and catalyst into a mixer having static elements which provide essentially uniform plug flow characteristics to the catalyzed mixture passing therethrough, maintained under pressure and providing sufficient residence time for completion of the polymerization, and controlling the polymer viscosity by introducing to the initial part of the static mixer reaction zone a low molecular weight triorganosilyldiorganopolysiloxane as a chain-stopper, and where the organo group is a monovalent hydrogen radical; (c) mixing into the reaction mixture an amount of a neutralizing agent effective to neutralize the basic catalyst and (d) passing the solution of the neutralizing agent and reaction mixture through a static mixer for completion of the neutralization.

Claim 17

A process as in claim 14, wherein the basic catalyst is selected from the group consisting of cesium hydroxide, potassium hydroxide, sodium hydroxide, cesium silanolate, potassium silanolate and sodium silanolate.

Claim 18

A process as in claim 15, wherein the basic catalyst is potassium silanolate.

Claim 19

A process as in claim 15, wherein the triorganosilyldiorganopolysiloxane chainstopper has the general formula, (CH.sub.3).sub.3 Si--[OSi(CH.sub.3).sub.2 ].sub.n --Si(CH.sub.3).sub.3 wherein n is a positive integer of approximately 3 or more.