Patent US4252908A successfully refreshed from Google Patents.
US4252908A
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Process for the preparation of phenol-formaldehyde foams
Assignee: Orkem SA
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Filing: 1979-05-21
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Granted: 1981-02-24
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Expires: 1999-05-21
Abstract
Abstract The present invention relates to a process for the preparation of phenol-formaldehyde foams by mixing a resol phase having a viscosity of between 8 and 60 poises and a novolac phase comprising a true novolac, a blowing agent, phenolsulphonic acid and, optionally, phenol, the relative amounts of resol phase and of novolac phase being such that the resol phase represents 45 to 75% by weight of the mixture.
Inventors
- 👤 Jean-Claude Paladini
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-03 22:21
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/04; C08J9/12; C08J9/14; C08J9/149; C08G; C08G8/00; C08G8/04; C08G8/08; C08G8/10; C08J9/0061; C08J9/141; C08J9/143; C08L; C08L61/00; C08L61/04; C08L61/06; C08J2361/00; C08J2361/04; C08J2361/06; C08J2361/08; C08J2361/10; C08J2461/00; C08J2461/04; C08J2461/06; C08J2461/08; C08J2461/10
Claims Analysis
Total Claims: 7
Claim 1
Independent Claim
296 words
Process for the preparation of phenol-formaldehyde foam which consisting of introducing a resol phase and a liquid anhydrous novolac phase into a mixer, mixing the resol phase and the novolac phase for a period of between about 5 and about 90 seconds to obtain a resin mixture, and subsequently spraying the resin mixture produced out of said mixer to obtain the foam, wherein the resol phase is homogeneous, has a viscosity, measured at 20°, of between 8 and 60 poises, and has a solids content of between 70 and 95% by weight, the resol contained in the said phase being obtained by polycondensation, by means of a basic catalyst, of phenol and formaldehyde in a molar ratio of between 1:1.5 and 1:3; the liquid novolac phase is a homogeneous and anhydrous essentially uncured liquid mixture which has a viscosity, measured at 20° C., of between about 5 and about 300 poises and contains from 10 to 35% by weight of a blowing agent which is a halogenated hydrocarbon selected from the group consisting of methylene chloride, chloroform, 1,1,1-trichloroethane, trichloroethylene, dichloroethane and mixtures thereof or a mixture of said halogenated hydrocarbon with ethanol, and from 70 to 90% by weight of a mixture comprising a true novolac resin obtained by polycondensation, by means of an acid catalyst, of a mixture of phenol and formaldehyde in a molar ratio of 2:1 to 6:1, phenolsulphonic acid in an amount of between 5 and 10% by weight relative to the resin mixture of resol phase and novolac phase and optionally, free phenol representing at most 30% by weight of the novolac phase; the relative amounts by weight of resol phase and of novolac phase being such that the resol phase represents 45 to 75% by weight of the resin mixture.
Claim 2
Dependent Claim
296 words
Process for the preparation of phenol-formaldehyde foam which consisting of introducing a resol phase and a liquid anhydrous novolac phase into a mixer, mixing the resol phase and the novolac phase for a period of between about 5 and about 90 seconds to obtain a resin mixture, and subsequently spraying the resin mixture produced out of said mixer to obtain the foam, wherein the resol phase is homogeneous, has a viscosity, measured at 20°, of between 8 and 60 poises, and has a solids content of between 70 and 95% by weight, the resol contained in the said phase being obtained by polycondensation, by means of a basic catalyst, of phenol and formaldehyde in a molar ratio of between 1:1.5 and 1:3; the liquid novolac phase is a homogeneous and anhydrous essentially uncured liquid mixture which has a viscosity, measured at 20° C., of between about 5 and about 300 poises and contains from 10 to 35% by weight of a blowing agent which is a halogenated hydrocarbon selected from the group consisting of methylene chloride, chloroform, 1,1,1-trichloroethane, trichloroethylene, dichloroethane and mixtures thereof or a mixture of said halogenated hydrocarbon with ethanol, and from 70 to 90% by weight of a mixture comprising a true novolac resin obtained by polycondensation, by means of an acid catalyst, of a mixture of phenol and formaldehyde in a molar ratio of 2:1 to 6:1, phenolsulphonic acid in an amount of between 5 and 10% by weight relative to the resin mixture of resol phase and novolac phase and optionally, free phenol representing at most 30% by weight of the novolac phase; the relative amounts by weight of resol phase and of novolac phase being such that the resol phase represents 45 to 75% by weight of the resin mixture.
Claim 3
Dependent Claim
58 words
Process according to claim 1, wherein the novolac phase contains from 16 to 23% by weight of a blowing agent, from 10 to 15% by weight of phenolsulphonic acid and from 60 to 70% by weight of a true novolac resin, and the proportion by weight of resol phase in the mixture is of the order of 50%.
Claim 4
Dependent Claim
74 words
Process according to claim 1, wherein the novolac phase contains from 16 to 23% by weight of a blowing agent, from 20 to 30% by weight of phenolsulphonic acid and from 50 to 60% by weight of a mixture containing 40 to 90% by weight of a true novolac resin and 60 to 10% by weight of phenol, and the proportion, by weight of resol phase in the mixture is between 65 and 75%.
Claim 5
Dependent Claim
24 words
Process according to claim 1, wherein the resol phase contains about 0.5 mol of urea per mol of free formaldehyde which it may contain.
Claim 6
Dependent Claim
25 words
Process according to claim 1, wherein the blowing agent is selected from amongst methylene chloride, chloroform, 1,1,1-trichloroethane, trichloroethylene, dichloroethane and the mixtures of these products.
Claim 7
Dependent Claim
26 words
Process according to claim 1, wherein the blowing agent is a mixture containing 40 parts by weight of ethanol per 60 parts by weight of trichloroethane.
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) | 1984-02-24 | 1984-08-25 | 1985-02-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-02-24 | 1988-08-25 | 1989-02-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-02-24 | 1992-08-25 | 1993-02-24 | $7700.00 | Window Closed / Lapsed |