Claims
- 1. A process aid which is prepared in situ in the presence of a polysiloxane gum comprising a reaction product of (a) 100 parts by weight of a cyclictrisiloxane of the formula, (RR'SiO).sub.3 where R and R' are selected from monovalent hydrocarbon radicals and halogenated monovalent hydrocarbon radicals; (b) at least 3 parts by weight of a hydroxy containing additive selected from the class consisting of H.sub.2 O and R.sup.2 OH where R.sup.2 is an alkyl radical of 1 to 3 carbon atoms and (c) at least 200 parts per million of a catalyst selected from the class consisting of Li OH, NH.sub.3, NH.sub.4 OH and R.sup.3 NH.sub.2 where R.sup.3 is a monovalent hydrocarbon radical.
- 2. The process aid of claim 1 wherein R is selected from the class consisting of alkyl radicals and aryl radicals of 1 to 8 carbon atoms and R' is selected from the class consisting of alkyl radicals, alkenyl radicals, aryl radicals and fluoroalkyl radicals of 1 to 8 atoms.
- 3. The process aid of claim 1 wherein there is present from 3 to 15 parts by weight of H.sub.2 O.
- 4. The process aid of claim 1 wherein there is present from 4.5 to 90 parts by weight of R.sup.2 OH.
- 5. The process aid of claim 1 where there is present from 500 to 20,000 parts per million of said catalyst.
- 6. The process aid of claim 5 wherein there is present from 4,000 to 10,000 parts per million of NH.sub.3.
- 7. A process for obtaining a process aid in the presence of a polysiloxane gum comprising placing a mixture of (a) 100 parts by weight of a cyclictrisiloxane of the formula,
- (RR'SiO).sub.3
- where R and R' are selected from monovalent hydrocarbon radicals and halogenated monovalent hydrocarbon radicals; (b) at least 3 parts by weight of a hydroxy-containing additive selected from the class consisting of H.sub.2 O and R.sup.2 OH where R.sup.2 is an alkyl radical of 1 to 3 carbon atoms; and (c) at least 200 parts per million of a catalyst selected from the class consisting of Li OH, NH.sub.3, NH.sub.4 OH and R.sup.3 NH.sub.2 where R.sup.3 is selected from monovalent hydrocarbon radicals in the presence of said polysiloxane gum and reacting said mixture.
- 8. The process of claim 7 which is carried out at a temperature in the range of 140.degree.-170.degree. C. for a period of time of at least 0.25 hours.
- 9. The process of claim 7 wherein R is selected from the class consisting of alkyl radicals and aryl radicals of 1 to 8 carbon atoms and R' is selected from the class consisting of alkyl radicals, alkenyl radicals, aryl radicals and fluoroalkyl radicals of 1 to 8 carbon atoms.
- 10. The process of claim 7 wherein there is present from 3 to 15 parts by weight of H.sub.2 O.
- 11. The process of claim 7 wherein there is present from 4.5 to 90 parts by weight of R.sup.2 OH.
- 12. The process of claim 7 wherein there is present from 500 to 20,000 parts per million of said catalyst.
- 13. The process of claim 12 wherein there is present from 4,000 to 10,000 parts per million of NH.sub.3.
- 14. A heat curable silicone rubber composition having an improved process aid comprising (a) 100 parts by weight of a diorganopolysiloxane having a viscosity of 1,000,000 to 200,000,000 centipoise at 25.degree. C. wherein the organo groups are selected from the class consisting of monovalent hydrocarbon radicals and halogenated monovalent hydrocarbon radicals; (b) from 5 to 200 parts by weight of filler; (c) from 0.1 to 10 parts of a curing catalyst; and (d) from 1 to 25 parts by weight of a process aid which is the reaction product of (i) 100 parts by weight of a cyclictrisiloxane of the formula,
- (RR'SiO).sub.3
- where R and R' are selected from monovalent hydrocarbon radicals and halogenated monovalent hydrocarbon radicals; (ii) at least 3 parts by weight of a hydroxy containing additive selected from the class consisting of H.sub.2 O and R.sup.2 OH where R.sup.2 is an alkyl radical of 1 to 3 carbon atoms and (iii) at least 200 parts per million of a catalyst selected from the class consisting of Li OH, NH.sub.3, NH.sub.4 OH and R.sup.3 NH.sub.2 where R.sup.3 is a monovalent hydrocarbon radical.
- 15. A process for preparing a process aid in the presence of a diorganopolysiloxane having a viscosity of 1,000,000 to 200,000,000 centipoise at 25.degree. C. where the organo groups are selected from the class consisting of monovalent hydrocarbon radicals and halogenated monovalent hydrocarbon radicals and a filler comprising (a) adding to said diorganopolysiloxane a mixture of (i) 100 parts by weight of a cyclictrisiloxane of the formula,
- (RR'SiO).sub.3
- where R and R' are selected from monovalent hydrocarbon radicals and halogenated monovalent hydrocarbon radicals; (ii) at least 3 parts by weight of a hydroxy containing additive selected from the class consisting of H.sub.2 O and R.sup.2 OH where R.sup.2 is an alkyl radical of 1 to 3 carbon atoms and (iii) at least 200 parts per million of a catalyst selected from the class consisting of Li OH, NH.sub.3, NH.sub.4 OH and R.sup.3 NH.sub.2 where R.sup.3 is a monovalent hydrocarbon radical (b) adding a filler; and (c) reacting the above (i), (ii) and (iii).
Parent Case Info
This application is a continuation of parent application Ser. No. 847,195 filed on Oct. 31, 1978, now abandoned.
US Referenced Citations (2)
Number |
Name |
Date |
Kind |
3560437 |
Szendrey |
Feb 1971 |
|
3925285 |
Newton |
Dec 1975 |
|
Continuations (1)
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Number |
Date |
Country |
Parent |
847195 |
Oct 1978 |
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