US4467053A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for producing an expandable silicone resin
Assignee: Rosemount Inc
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Filing: 1983-12-28
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Granted: 1984-08-21
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Expires: 2003-12-28
Abstract
Abstract A process for the production of an expandable silicone resin includes reacting a substantial amount of the silanol (SiOH) groups present in the resin to form siloxane bonds and water, and heating the resin to a temperature above the resin's melting point, at which chemical reaction (condensation) of the silanol groups occur. The reaction increases the molecular weight of the resin and decreases the amount of water that must be removed during a subsequent foaming step, thereby controlling the rate and extent of foaming which can occur. The resin is solidified, pulverized and size-reduced to a powder form. The resin powder is blended with a minor amount of a particulate inert filler which is coated with a silicone resin curing catalyst and also with a minor amount of blowing agent (powder). The dry powder blend is then thermally fused for a closely-controlled, short duration, time at a temperature near the lower end of the blowing agent's gas-generating temperature range. The fused mass is ground to a powdered form to produce an expandable resin.
Inventors
- 👤 Richard A. Markle
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 07:41
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/02; C08J9/0066; C08J9/04; C08J9/06; C08J9/10; C08J2383/00; C08J2383/04
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
163 words
A process for the production of an expandable silicone resin containing powder comprising: heating a silicone resin having a formula of: R n SiO 4-n/2 where R is selected from the group consisting of methyl, ethyl, vinyl and phenyl radicals and n has an average value of from 1 to 1.5 inclusive, to a temperature to condense the latent water into free water until approximately 20% to 70% of the latent water has been condensed and evaporated to effect an increase in molecular weight of the silicone resin; blending a particulate inert filler and a blowing agent in an environment in which the blowing agent does not generate substantial amounts of gas with the silicone resin to form a mixture, the blending of the blowing agent and inert filler with the resin being either separately or simultaneously; cooling the mixture to a solidified mass; reducing the solidified mass into a powder which expands when heated above the gas-generating temperature of the blowing agent.
Claim 2
Dependent Claim
163 words
A process for the production of an expandable silicone resin containing powder comprising: heating a silicone resin having a formula of: R n SiO 4-n/2 where R is selected from the group consisting of methyl, ethyl, vinyl and phenyl radicals and n has an average value of from 1 to 1.5 inclusive, to a temperature to condense the latent water into free water until approximately 20% to 70% of the latent water has been condensed and evaporated to effect an increase in molecular weight of the silicone resin; blending a particulate inert filler and a blowing agent in an environment in which the blowing agent does not generate substantial amounts of gas with the silicone resin to form a mixture, the blending of the blowing agent and inert filler with the resin being either separately or simultaneously; cooling the mixture to a solidified mass; reducing the solidified mass into a powder which expands when heated above the gas-generating temperature of the blowing agent.
Claim 3
Dependent Claim
22 words
The process of claim 1 wherein R is methyl and phenyl substituents in a mole ratio of approximately 0.67/1 to 1.5/1.0, phenyl/methyl.
Claim 4
Dependent Claim
11 words
The process of claim 1 wherein the filler is diatomaceous earth.
Claim 5
Dependent Claim
15 words
The process of claim 3 wherein the diatomaceous earth has a pH of approximately 7.0.
Claim 6
Dependent Claim
16 words
The process of claim 1 and further including coating the inert filler with a cross-linking catalyst.
Claim 7
Dependent Claim
34 words
The process of claim 5 and further including cooling the resin after initially heating and reducing in size the resin to a powdered form and dry blending the catalyst-coated filler with the powdered resin.
Claim 8
Dependent Claim
25 words
The process of claim 6 and further including dry blending the blowing agent and the resin and the catalyst-coated inert filler to form a mixture.
Claim 9
Dependent Claim
31 words
The process of claim 7 and further including fusing the mixture by heating to a temperature above the melting point of the resin but less than the blowing agent's gas-generating temperature.
Claim 10
Dependent Claim
23 words
The process of claim 7 wherein the temperature for fusing the blend is approximately in the range of 240° F. to 270° F.
Claim 11
Dependent Claim
11 words
The process of claim 5 wherein the catalyst is choline octoate.
Claim 12
Dependent Claim
13 words
The process of claim 1 wherein the blowing agent is dinitroso pentamethylene tetramine.
Claim 13
Dependent Claim
23 words
The process of claim 1 wherein the silicone resin is initially heated to approximately 350° F.±5° F. for approximately 10 to 90 minutes.
References Cited (Backward Citations)
US2803606A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1987-08-21 | 1988-02-20 | 1988-08-21 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-08-21 | 1992-02-20 | 1992-08-21 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-08-21 | 1996-02-20 | 1996-08-21 | $7700.00 | Window Closed / Lapsed |