Patent US3937684A successfully refreshed from Google Patents.
← Back to Patent Explorer
US3937684A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing high molecular weight diorganopolysiloxanes for use in heat vulcanizable silicone rubber compositions

Assignee: General Electric Co
•
Filing: 1974-04-24
•
Granted: 1976-02-10
•
Expires: 1994-04-24
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A process for producing diorganopolysiloxane gums having a viscosity from 1,000 to 100,000,000 centipoise at 25°C, where at least one of the organo substituent groups on the silicon atoms is an aliphatic radical of more than three carbon atoms comprising reacting a cyclic tetrasiloxane or a mixture of cyclic tetrasiloxanes at a temperature in the range of 0° to 90° C and in the presence of 5 to 300 parts per million of a catalyst selected from the class consisting of cesium hydroxide and ##EQU1## where R 2 is selected from the class consisting of alkyl radicals of 1 to 8 carbon atoms, cycloalkyl radicals of 4 to 8 carbon atoms and phenyl, B is selected from the class consisting of nitrogen and phosphorous, R 3 is selected from the class consisting of alkyl radicals of 1 to 8 carbon atoms, cycloalkyl radicals of 4 to 8 carbon atoms, phenyl, siloxane chains of the unit formula R a 4 SiO 4 -a/2 and mixtures thereof, where R 4 is selected from the class consisting of monovalent hydrocarbon radicals and halogenated monovalent hydrocarbon radicals, and a varies from 1.5 to 2.5.

Inventors

  • 👤 John S. Razzano

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-26 05:36
CPC Classifications
C; C08; C08G; C08G77/00; C08G77/04; C08G77/06; C08G77/08; C08G77/22; C08G77/24

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 382 words
A process for producing diorganopolysiloxane polymers having a viscosity from 1,000 to 200,000,000 centipoise at 25°C where at least one of the organo groups is an aliphatic or haloaliphatic radical of 3 carbon atoms or more consisting essentially of (a) hydrolyzing in a water and a water-immiscible organic solvent mixture, a silane of the formula, R R' SiX.sub.2 and mixtures of said silane, where R is selected from the class consisting of methyl, ethyl, vinyl and phenyl and R' is selected from the class consisting of alkyl radicals, halogenated alkyl radicals and cycloalkyl radicals of 3 to 8 carbon atoms, X is halogen; (b) separating the water and water-immiscible organic solvent from the hydrolyzate; (c) adding 0.5 to 2% by weight of a catalyst selected from the class consisting of KOH, NaOH, and CsOH to the hydrolyzate and heating the hydrolyzate to 150°C to 200°C; (d) removing overhead a mixture of cyclic polysiloxanes and transferring such cyclic polysiloxanes into a distillation column; (e) separating by distillation at a temperature of 80°-200°C and 1 to 50 mm of Hg vacuum essentially pure tetracyclic polysiloxanes of the formula, (R R' SiO).sub.4 and mixtures thereof, where R and R' are as previously defined; (f) heating the tetracyclic polysiloxanes above 100°C with a nitrogen purge to reduce the water content to less than 10 parts per million; (g) reacting the cyclic tetrapolysiloxanes at a temperature in the range of 0° to 90°C in the presence of 5 to 300 parts per million of a catalyst selected from the class consisting of CsOH and ##EQU5## where R 2 is selected from the class consisting of alkyl radicals of 1 to 8 carbon atoms, cycloalkyl radicals of 4 to 8 carbon atoms and phenyl, B is selected from the class consisting of nitrogen and phosphorous, R 3 is selected from the class consisting of alkyl radicals of 1 to 8 carbon atoms, cycloalkyl radicals of 4 to 8 carbon atoms, phenyl, siloxane chains of the unit formula, R a 4 SiO.sub.(4 -a )/2 and mixtures thereof, where R 4 is selected from the class consisting of monovalent hydrocarbon radicals and halogenated monovalent hydrocarbon radicals, a varies from 1.5 to 2.5; until equilibration is reached and (h) neutralizing the catalyst in the reaction mixture after equilibrium has been reached.
Claim 2
Dependent Claim 382 words
A process for producing diorganopolysiloxane polymers having a viscosity from 1,000 to 200,000,000 centipoise at 25°C where at least one of the organo groups is an aliphatic or haloaliphatic radical of 3 carbon atoms or more consisting essentially of (a) hydrolyzing in a water and a water-immiscible organic solvent mixture, a silane of the formula, R R' SiX.sub.2 and mixtures of said silane, where R is selected from the class consisting of methyl, ethyl, vinyl and phenyl and R' is selected from the class consisting of alkyl radicals, halogenated alkyl radicals and cycloalkyl radicals of 3 to 8 carbon atoms, X is halogen; (b) separating the water and water-immiscible organic solvent from the hydrolyzate; (c) adding 0.5 to 2% by weight of a catalyst selected from the class consisting of KOH, NaOH, and CsOH to the hydrolyzate and heating the hydrolyzate to 150°C to 200°C; (d) removing overhead a mixture of cyclic polysiloxanes and transferring such cyclic polysiloxanes into a distillation column; (e) separating by distillation at a temperature of 80°-200°C and 1 to 50 mm of Hg vacuum essentially pure tetracyclic polysiloxanes of the formula, (R R' SiO).sub.4 and mixtures thereof, where R and R' are as previously defined; (f) heating the tetracyclic polysiloxanes above 100°C with a nitrogen purge to reduce the water content to less than 10 parts per million; (g) reacting the cyclic tetrapolysiloxanes at a temperature in the range of 0° to 90°C in the presence of 5 to 300 parts per million of a catalyst selected from the class consisting of CsOH and ##EQU5## where R 2 is selected from the class consisting of alkyl radicals of 1 to 8 carbon atoms, cycloalkyl radicals of 4 to 8 carbon atoms and phenyl, B is selected from the class consisting of nitrogen and phosphorous, R 3 is selected from the class consisting of alkyl radicals of 1 to 8 carbon atoms, cycloalkyl radicals of 4 to 8 carbon atoms, phenyl, siloxane chains of the unit formula, R a 4 SiO.sub.(4 -a )/2 and mixtures thereof, where R 4 is selected from the class consisting of monovalent hydrocarbon radicals and halogenated monovalent hydrocarbon radicals, a varies from 1.5 to 2.5; until equilibration is reached and (h) neutralizing the catalyst in the reaction mixture after equilibrium has been reached.
Claim 3
Dependent Claim 32 words
The process of claim 1 wherein in step (a) the amount of water is controlled such that there is formed 20% by weight of an aqueous halogen acid solution during the hydrolysis.
Claim 4
Dependent Claim 67 words
The process of claim 1 wherein the catalyst is neutralized in step (h) with an ingredient selected from the class consisting of phosphoric acid and of the formula, R.sub.b.sup.6 SiX.sub.4.sub.-b where R 6 is selected from the class consisting of alkyl radicals, cycloalkyl radicals, vinyl radicals and phenyl radicals, X is selected from the class consisting of bromine and chlorine and b varies from 0 to 3.
Claim 5
Dependent Claim 41 words
The process of claim 1 wherein after step (h) further comprising heating the reaction mixture to 150° to 200°C at a vacuum of 1 to 100 mm of Hg to remove all volatiles so as to result in the desired product.
Claim 6
Dependent Claim 26 words
The process of claim 1 wherein in step (g) the reaction is carried out for a period of time varying from 1/2 hour to 10 hours.
Claim 7
Dependent Claim 34 words
The process of claim 1 wherein after step (f) the tetracyclicpolysiloxanes and mixtures thereof contain less than 20 parts per million of trifunctional siloxanes, and less than 200 parts per million of monofunctional siloxanes.
Claim 8
Dependent Claim 28 words
The process of claim 1 wherein R' is R 5 CH 2 CH 2 -- and R 5 is a perfluoroalkyl radical of 1 to 6 carbon atoms.

References Cited (Backward Citations)

US3132167A Cited
US3598851A Cited
US3481898A Cited
US3661962A Cited
US3779987A Cited
US3842110A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-02-09 1979-08-11 1980-02-10 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-02-09 1983-08-11 1984-02-10 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-02-09 1987-08-11 1988-02-10 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag