US4337318A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the total pre-expansion of polyurethane foam
Assignee: Individual
•
Filing: 1980-09-30
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Granted: 1982-06-29
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Expires: 2000-09-30
Abstract
Abstract The present invention provides a method of utilizing polyurethane foam for insulation purposes in existing walls and other areas without expanding the existing structure. Conventional polyurethane foam post-expands, causing pressures as high as 6 p.s.i., which results in swelling and expanding of existing wall structures. The process of the present invention places the polyurethane foam into its final position in a totally pre-expanded form, making it possible to insulate homes, office buildings, and any other existing structure with foam having a density as low as 0.5 lb. per cu. ft. with no distortion of even the weakest type of structure.
Inventors
- 👤 Earl N. Doyle
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 11:09
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/04; C08J9/12; C08J2375/00; C08J2375/04; Y; Y10; Y10S; Y10S521/00; Y10S521/917
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
143 words
A process for the production of low density polyurethane foam in the absence of post-expansion, said process comprising the steps of: (a) mixing together in a mixing zone at ambient temperature (i) a first component comprising polymeric diisocyanate having a functionallty within the range of approximately 2.2 to 2.9, (ii) a second component comprising a blend of polyol, surfactant, and catalyst, and (iii) a blowing agent comprising a gas having a boiling point below approximately -100° F. at atmospheric pressure, the mixture being subjected in said mixing zone to a pressure sufficient to maintain said blowing agent in the liquid state at ambient temperature, said mixture being substantially free of water; (b) ejecting said mixture from said mixing zone to atmospheric pressure, thereby completely and instantaneously vaporizing said blowing agent and providing total expansion of said mixture, and (c) curing the resulting foam.
Claim 2
Dependent Claim
143 words
A process for the production of low density polyurethane foam in the absence of post-expansion, said process comprising the steps of: (a) mixing together in a mixing zone at ambient temperature (i) a first component comprising polymeric diisocyanate having a functionallty within the range of approximately 2.2 to 2.9, (ii) a second component comprising a blend of polyol, surfactant, and catalyst, and (iii) a blowing agent comprising a gas having a boiling point below approximately -100° F. at atmospheric pressure, the mixture being subjected in said mixing zone to a pressure sufficient to maintain said blowing agent in the liquid state at ambient temperature, said mixture being substantially free of water; (b) ejecting said mixture from said mixing zone to atmospheric pressure, thereby completely and instantaneously vaporizing said blowing agent and providing total expansion of said mixture, and (c) curing the resulting foam.
Claim 3
Dependent Claim
27 words
The process of claim 1 wherein said blowing agent is selected from the group consisting of carbon dioxide, nitrogen, helium, tetrafluoroethane, fluoroform, hexafluoroethane, chlorotrifluoromethane, and mixtures thereof.
Claim 4
Dependent Claim
12 words
The process of claim 2 wherein said blowing agent is carbon dioxide.
Claim 5
Dependent Claim
23 words
The process of claim 1 wherein said mixture is subjected in said mixing zone to a pressure of at least approximately 1000 p.s.i.
Claim 6
Dependent Claim
24 words
The process of claim 1 wherein said polyurethane form has a density within the range of approximately 0.5 to 6 lbs. per cu. ft.
Claim 7
Dependent Claim
19 words
The process of claim 1 wherein said first component and said second component are provided in substantially equal volumes.
Claim 8
Dependent Claim
135 words
A process for the production of low density polyurethane foam in the absence of post-expansion, said process comprising the steps of: (a) mixing together in a mixing zone at ambient temperature (i) a first component comprising polymeric diisocyanate having a functionality within the range of approximately 2.2 to 2.9, (ii) a second component comprising a blend of polyol, surfactant, and catalyst, and (iii) carbon dioxide, the mixture being subjected in said mixing zone to a pressure of at least approximately 1000 p.s.i. in order to maintain said carbon dioxide in the liquid state at ambient temperature, said mixture being substantially free of water; (b) ejecting said mixture from said mixing zone to atmospheric pressure, thereby completely and instantaneously vaporizing said carbon dioxide and providing total expansion of said mixture; and (c) curing the resulting foam.
Claim 9
Dependent Claim
135 words
A process for the production of low density polyurethane foam in the absence of post-expansion, said process comprising the steps of: (a) mixing together in a mixing zone at ambient temperature (i) a first component comprising polymeric diisocyanate having a functionality within the range of approximately 2.2 to 2.9, (ii) a second component comprising a blend of polyol, surfactant, and catalyst, and (iii) carbon dioxide, the mixture being subjected in said mixing zone to a pressure of at least approximately 1000 p.s.i. in order to maintain said carbon dioxide in the liquid state at ambient temperature, said mixture being substantially free of water; (b) ejecting said mixture from said mixing zone to atmospheric pressure, thereby completely and instantaneously vaporizing said carbon dioxide and providing total expansion of said mixture; and (c) curing the resulting foam.
Claim 10
Dependent Claim
24 words
The process of claim 7 wherein said polyurethane foam has a density within the range of approximately 0.5 to 6 lbs. per. cu. ft.
Claim 11
Dependent Claim
20 words
The process of claim 7 wherein said mixture comprises substantially equal volumes of said first component and said second component.
Claim 12
Dependent Claim
28 words
The process of claim 7 wherein said mixture in said mixing zone comprises approximately 10 to 25 percent by volume of said carbon dioxide in the liquid state.
Claim 13
Dependent Claim
182 words
A process for the production, in the absence of post-expansion, of polyurethane foam having a density within the range of approximately 0.5 to 6 lbs. per cu. ft., said process comprising the steps of: (a) mixing together in a mixing zone at ambient temperature (i) a first component comprising polymeric diisocyanate having a functionality within the range of approximately 2.2 to 2.9, (ii) a second component comprising a blend of polyol, surfactant, and catalyst, and (iii) carbon dioxide, the mixture being subjected in said mixing zone to a pressure of at least approximately 1000 p.s.i. in order to maintain said carbon dioxide in the liquid state at ambient temperature, said mixture comprising substantially equal volumes of said first component and said second component, said mixture further comprising approximately 10 to 25 percent by volume of said carbon dioxide in the liquid state, and said mixture being substantially free of water; (b) ejecting said mixture from said mixing zone to atmospheric pressure, thereby completely and instantaneously vaporizing said blowing agent and providing total expansion of said mixture; and (c) curing the resulting foam.
Claim 14
Dependent Claim
182 words
A process for the production, in the absence of post-expansion, of polyurethane foam having a density within the range of approximately 0.5 to 6 lbs. per cu. ft., said process comprising the steps of: (a) mixing together in a mixing zone at ambient temperature (i) a first component comprising polymeric diisocyanate having a functionality within the range of approximately 2.2 to 2.9, (ii) a second component comprising a blend of polyol, surfactant, and catalyst, and (iii) carbon dioxide, the mixture being subjected in said mixing zone to a pressure of at least approximately 1000 p.s.i. in order to maintain said carbon dioxide in the liquid state at ambient temperature, said mixture comprising substantially equal volumes of said first component and said second component, said mixture further comprising approximately 10 to 25 percent by volume of said carbon dioxide in the liquid state, and said mixture being substantially free of water; (b) ejecting said mixture from said mixing zone to atmospheric pressure, thereby completely and instantaneously vaporizing said blowing agent and providing total expansion of said mixture; and (c) curing the resulting foam.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-06-28 | 1985-12-28 | 1986-06-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-06-28 | 1989-12-28 | 1990-06-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-06-28 | 1993-12-28 | 1994-06-29 | $7700.00 | Window Closed / Lapsed |