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Method of preparing non-friable rigid polyurethane foam

Assignee: Air Products and Chemicals Inc
•
Filing: 1975-01-30
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Granted: 1976-08-17
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Expires: 1995-01-30
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Abstract

Abstract The friability of rigid polyurethane foams prepared using a chlorine- or bromine-containing polyol is significantly reduced or eliminated by the use of a dimethyltin-S,S'-bis(alkylmercaptocarboxylate) as the polymerization catalyst.

Inventors

  • 👤 Robert V. Russo

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-05 22:51
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/40; C08G18/48; C08G18/487; C08G18/4883; C08G18/08; C08G18/16; C08G18/161; C08G18/163; C08G18/165; C08G18/22; C08G18/24; C08G18/242; C08G18/50; C08G18/5003; C08G18/5006

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 268 words
A method for preparing a flame retardant, rigid polyurethane foam of reduced friability from halogen-containing polyols by reacting a. 100 parts of a saccharide based polyol containing 4 hydroxyl groups, between 25 and 50% by weight of chlorine or bromine and exhibiting a hydroxyl number of between 175 and 800, the polyol being derived from the reaction of a bromine- or chlorine-containing olefin oxide containing between 3 and 12 carbon atoms with (1) a saccharide selected from the group consisting of dextrose, sucrose, α-methyl glucoside, (2) a reaction product of said saccharide with water or an alcohol containing between 2 and 4 hydroxyl radicals, or (3) said reaction product which has subsequently been oxyalkylated, b. a polyfunctional isocyanate exhibiting a functionality of between 2.2 and 2.8, wherein the total number of equivalents of isocyanate is between 0.95 and 1.2 times the number of equivalents of hydroxyl radicals present in said polyol, said reaction being conducted in the presence of between 20 and 40 parts of a foaming agent selected from the group consisting of halogenated aliphatic hydrocarbons exhibiting a boiling point of between -30° and 80°C., between 0.05 and 0.5 part of a polymerization catalyst of the formula (CH 3 ) 2 Sn(SR 1 COOR 2 ) 2 wherein R 1 is an alkylene radical containing between 1 and 12 carbon atoms and R 2 is selected from the group consisting of alkyl radicals containing between 1 and 20 carbon atoms, cycloalkyl, aryl, alkaryl and aralkyl radicals, between 0.2 and 1.5 parts of a tertiary amine cocatalyst and between 0.5 and 3 parts of a silicone oil surfactant.
Claim 2
Independent Claim 268 words
A method for preparing a flame retardant, rigid polyurethane foam of reduced friability from halogen-containing polyols by reacting a. 100 parts of a saccharide based polyol containing 4 hydroxyl groups, between 25 and 50% by weight of chlorine or bromine and exhibiting a hydroxyl number of between 175 and 800, the polyol being derived from the reaction of a bromine- or chlorine-containing olefin oxide containing between 3 and 12 carbon atoms with (1) a saccharide selected from the group consisting of dextrose, sucrose, α-methyl glucoside, (2) a reaction product of said saccharide with water or an alcohol containing between 2 and 4 hydroxyl radicals, or (3) said reaction product which has subsequently been oxyalkylated, b. a polyfunctional isocyanate exhibiting a functionality of between 2.2 and 2.8, wherein the total number of equivalents of isocyanate is between 0.95 and 1.2 times the number of equivalents of hydroxyl radicals present in said polyol, said reaction being conducted in the presence of between 20 and 40 parts of a foaming agent selected from the group consisting of halogenated aliphatic hydrocarbons exhibiting a boiling point of between -30° and 80°C., between 0.05 and 0.5 part of a polymerization catalyst of the formula (CH 3 ) 2 Sn(SR 1 COOR 2 ) 2 wherein R 1 is an alkylene radical containing between 1 and 12 carbon atoms and R 2 is selected from the group consisting of alkyl radicals containing between 1 and 20 carbon atoms, cycloalkyl, aryl, alkaryl and aralkyl radicals, between 0.2 and 1.5 parts of a tertiary amine cocatalyst and between 0.5 and 3 parts of a silicone oil surfactant.
Claim 3
Dependent Claim 20 words
A method for preparing a rigid polyurethane foam as described in claim 1, wherein the polymerization catalyst is a dimethyltin-S,S'-bis(alkylmercaptoacetate).
Claim 4
Dependent Claim 20 words
A method for preparing a rigid polyurethane foam as described in claim 2 wherein the polymerization catalyst is dimethyltin-S,S'-bis(isooctyl mercaptoacetate).
Claim 5
Dependent Claim 20 words
A method for preparing a rigid polyurethane foam as described in claim 1 wherein the chlorine-containing olefin oxide is 4,4,4-trichloro-1,2-epoxybutane.
Claim 6
Dependent Claim 22 words
A method for preparing a rigid polyurethane foam as described in claim 1 wherein the polyfunctional isocyanate is a polyphenylene polymethylene isocyanate.
Claim 7
Dependent Claim 23 words
A method for preparing a rigid polyurethane foam as described in claim 1 wherein the foaming agent contains only carbon, chlorine and fluorine.
Claim 8
Dependent Claim 19 words
A method for preparing a rigid polyurethane foam as described in claim 6 wherein the foaming agent is trichlorofluoromethane.

References Cited (Backward Citations)

US3582501A Cited
US3726855A Cited
US3732176A Cited
US3808162A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-08-17 1980-02-16 1980-08-17 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-08-17 1984-02-16 1984-08-17 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-08-17 1988-02-16 1988-08-17 $7700.00 Window Closed / Lapsed

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