US4273882A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Preparation of thermally stable rigid polyurethane foam
Assignee: Arch Chemicals Inc
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Filing: 1980-06-02
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Granted: 1981-06-16
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Expires: 2000-06-02
Abstract
Abstract A process for the preparation of rigid polyurethane foams which are relatively stable at elevated temperatures involves reacting a polyether polyol reactant with an organic polyisocyanate reactant in the presence of a foaming agent comprising water. The polyol reactant is a select combination of three polyols and is effective in improving the thermal stability of the resulting foam without appreciably affecting its other physical properties.
Inventors
- 👤 Robert J. Raynor
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 02:04
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/40; C08G18/48; C08G18/4804; C08G18/482; C08G2110/00; C08G2110/0025; C08G2110/0041; C08G2110/005; C08G2110/0083
Claims Analysis
Total Claims: 12
Claim 1
Independent Claim
335 words
A process for preparing a rigid polyurethane foam which comprises reacting a polyether polyol reactant with an organic polyisocyanate reactant in the presence of a foaming agent having a proportion of water ranging from about 2 to about 44 parts by weight per 100 parts of the total polyol reactant, said proportion being effective in promoting the formation of urea structures to enhance the thermal stability of said foam, said polyether polyol reactant including: a main polyol having a hydroxyl number of about 250-650 and being the product of reacting a mixture of a carbohydrate and a member selected from the group consisting of ethylene diamine, the ethanolamines and a mixture thereof, with an oxide selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide and a mixture thereof, said member being employed in a molar ratio ranging from about 1 to about 12 moles per mole of said carbohydrate; a first supplemental polyol having a hydroxyl number of about 50-250 and being the product of reacting an aliphatic diol, triol or a mixture thereof with an alkylene oxide having 2-4 carbon atoms; and a second supplemental polyol having a hydroxyl number of about 300-800 and being an adduct of ethylene oxide and an amine selected from the group consisting of an aliphatic amine having 1-8 carbon atoms, an aromatic primary amine having 6-8 carbon atoms, an alkanolamine in which each alkanol group contains 2-5 carbon atoms, and a mixture thereof; and wherein: said main polyol is employed in a proportion of from about 30 to about 80 percent, said first supplemental polyol is employed in a proportion of from about 35 to about 10 percent, and said second supplemental polyol is employed in a proportion of from about 35 to about 10 percent, all percentages being based upon the total weight of said polyol reactant; and said polyisocyanate reactant is used in an amount so as to provide about 1.0 to about 4.0 NCO groups per hydroxy group in the reaction system.
Claim 2
Dependent Claim
335 words
A process for preparing a rigid polyurethane foam which comprises reacting a polyether polyol reactant with an organic polyisocyanate reactant in the presence of a foaming agent having a proportion of water ranging from about 2 to about 44 parts by weight per 100 parts of the total polyol reactant, said proportion being effective in promoting the formation of urea structures to enhance the thermal stability of said foam, said polyether polyol reactant including: a main polyol having a hydroxyl number of about 250-650 and being the product of reacting a mixture of a carbohydrate and a member selected from the group consisting of ethylene diamine, the ethanolamines and a mixture thereof, with an oxide selected from the group consisting of ethylene oxide, propylene oxide, butylene oxide and a mixture thereof, said member being employed in a molar ratio ranging from about 1 to about 12 moles per mole of said carbohydrate; a first supplemental polyol having a hydroxyl number of about 50-250 and being the product of reacting an aliphatic diol, triol or a mixture thereof with an alkylene oxide having 2-4 carbon atoms; and a second supplemental polyol having a hydroxyl number of about 300-800 and being an adduct of ethylene oxide and an amine selected from the group consisting of an aliphatic amine having 1-8 carbon atoms, an aromatic primary amine having 6-8 carbon atoms, an alkanolamine in which each alkanol group contains 2-5 carbon atoms, and a mixture thereof; and wherein: said main polyol is employed in a proportion of from about 30 to about 80 percent, said first supplemental polyol is employed in a proportion of from about 35 to about 10 percent, and said second supplemental polyol is employed in a proportion of from about 35 to about 10 percent, all percentages being based upon the total weight of said polyol reactant; and said polyisocyanate reactant is used in an amount so as to provide about 1.0 to about 4.0 NCO groups per hydroxy group in the reaction system.
Claim 3
Dependent Claim
13 words
A polyurethane foam prepared according to the process as recited in claim 1.
Claim 4
Dependent Claim
71 words
The process as recited in claim 1, wherein: said first supplemental polyol has a hydroxyl number of about 100-150, and is an oxypropylated or oxypropylated then oxyethylated diol or triol; and said second supplemental polyol has a hydroxyl number of about 450-700, and wherein said aliphatic amine is a diamine having 2-4 carbon atoms, said aromatic amine is toluene diamine, and said alkanolamine is an ethanolamine, a propanolamine or an ethanolpropanolamine.
Claim 5
Dependent Claim
15 words
The process as recited in claim 1, wherein said foaming agent consists essentially of water.
Claim 6
Dependent Claim
13 words
A polyurethane foam prepared according to the process as recited in claim 4.
Claim 7
Dependent Claim
31 words
The process as recited in claim 4, wherein said foaming agent is employed in a proportion of about 6-8 parts per every 100 parts by weight of said polyether polyol reactant.
Claim 8
Dependent Claim
52 words
The process as recited in claim 6, wherein said polyether polyol reactant includes: from about 40 to about 60 weight percent of said main polyol, from about 30 to about 20 weight percent of said first supplemental polyol, and from about 30 to about 20 weight percent of said second supplemental polyol.
Claim 9
Dependent Claim
60 words
The process as recited in claim 7, wherein: said main polyol is the product of reacting propylene oxide with a mixture of sucrose and diethanolamine; said first supplemental polyol is prepared by the sequential oxyalkylation of glycerol, first with propylene oxide and then with ethylene oxide; and said second supplemental polyol is an adduct of ethylene oxide and an ethanolamine.
Claim 10
Dependent Claim
15 words
The process as recited in claim 8, wherein said reaction mixture comprises a silicon-based surfactant.
Claim 11
Dependent Claim
21 words
The process as recited in claim 9, wherein said organic polyisocyanate reactant is toluene diisocyanate, polymethylene polyphenylisocyanate, or a mixture thereof.
Claim 12
Dependent Claim
13 words
A polyurethane foam prepared according to the process as recited in claim 10.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1984-06-15 | 1984-12-15 | 1985-06-16 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-06-15 | 1988-12-15 | 1989-06-16 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-06-15 | 1992-12-15 | 1993-06-16 | $7700.00 | Window Closed / Lapsed |