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US3933693A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of flame retardant flexible polyurethane foams

Assignee: Foamex LP
•
Filing: 1974-06-24
•
Granted: 1976-01-20
•
Expires: 1994-06-24
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Abstract

Abstract Flame retardant flexible polyurethane foams having a porosity in the range between 0.5 and 10 cubic feet per minute and meeting all of the requirements of Motor Vehicle Safety Standard Docket 302 may be produced from tolylene diisocyanate (which is a mixture of the 2,4- and 2,6-isomers) and polyether polyols without downgrading the flexibility or the porosity of the foam by (a) using in the polymerization reaction a tolylene diisocyanate in which the 2,4- to 2,6-isomer ratio is such that the tolylene diisocyanate contains not more than about 76 percent by weight of the 2,4-isomer, and (b) incorporating into the reaction medium prior to polymerization from about 1 to about 8 percent by weight of dibromoneopentyl glycol in a form such that the dibromoneopentyl glycol can be polymerized with the other reactants in the foam matrix, the weight of the dibromoneopentyl glycol being based on the weight of the polyether polyol used in the polymerization reaction. Best results have been obtained when the dibromoneopentyl glycol is incorporated in the reaction medium, either in the form of a dispersion or a solution of dibromoneopentyl glycol in the polyether polyol, using a tolylene diisocyanate in which the 2,4- to 2,6-isomer ratio is such that the tolylene diisocyanate contains 72.5 ± 2 percent by weight of the 2,4-isomer and 27.5 ± 2 percent by weight of the 2,6-isomer.

Inventors

  • 👤 David C. Priest
  • 👤 John E. Brandien, deceased

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 23:48
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/30; C08G18/38; C08G18/3802; C08G18/3804; C08G18/3806; C08G18/381; C08G18/65; C08G18/66; C08G18/6666; C08G18/70; C08G18/72; C08G18/74; C08G18/76; C08G18/7614; C08G18/7621; C08G2110/00; C08G2110/0008; C08G2110/0041; C08G2110/005; C08G2110/0083; Y; Y10; Y10S; Y10S521/00; Y10S521/914

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 125 words
In a process for producing flexible polyurethane foams having a porosity in the range from about 0.5 to about 10 cubic feet per minute, in which an isomeric mixture of 2,4- and 2,6-tolylene diisocyanate is reacted with a polyether polyol in the presence of a small amount of water and a catalytic amount of a polymerization catalyst, the improvement which comprises: a. reacting the polyether polyol with a sufficient amount of an isomeric mixture of tolylene diisocyanate which contains not more than about 76 percent by weight of the 2,4-isomer, and b. incorporating into the reaction mixture prior to polymerization from about 1 to about 8 percent by weight of dibromoneopentyl glycol based on the weight of the polyether polyol used in the polymerization reaction.
Claim 2
Dependent Claim 125 words
In a process for producing flexible polyurethane foams having a porosity in the range from about 0.5 to about 10 cubic feet per minute, in which an isomeric mixture of 2,4- and 2,6-tolylene diisocyanate is reacted with a polyether polyol in the presence of a small amount of water and a catalytic amount of a polymerization catalyst, the improvement which comprises: a. reacting the polyether polyol with a sufficient amount of an isomeric mixture of tolylene diisocyanate which contains not more than about 76 percent by weight of the 2,4-isomer, and b. incorporating into the reaction mixture prior to polymerization from about 1 to about 8 percent by weight of dibromoneopentyl glycol based on the weight of the polyether polyol used in the polymerization reaction.
Claim 3
Dependent Claim 39 words
A process for producing flame retardant flexible polyurethane foams according to claim 1, in which the tolylene diisocyanate used in the polymerization reaction has a 2,4-isomer content in the range from about 68 to about 76 percent by weight.
Claim 4
Dependent Claim 43 words
A process for producing flame retardant flexible polyurethane foams according to claim 1, in which the tolylene diisocyanate used in the polymerization reaction contains 72.5 ± 2 percent by weight of the 2,4-isomer and 27.5 ± 2 percent by weight of the 2,6-isomer.
Claim 5
Dependent Claim 37 words
A process for producing flame retardant flexible polyurethane foams according to claim 1, in which the dibromoneopentyl glycol is incorporated in the reaction medium in the form of a dispersion of dibromoneopentyl glycol in the polyether polyol.
Claim 6
Dependent Claim 37 words
A process for producing flame retardant flexible polyurethane foams according to claim 1, in which the dibromoneopentyl glycol is incorporated in the reaction medium in the form of a solution of dibromoneopentyl glycol in the polyether polyol.
Claim 7
Dependent Claim 37 words
A process for producing flame retardant flexible polyurethane foams according to claim 1, in which the polyether polyol is a poly(propylene oxide/ethylene oxide) triol having a molecular weight in the range from about 250 to about 6,500.
Claim 8
Dependent Claim 61 words
A process for producing flame retardant flexible polyurethane foams according to claim 1, in which from about 1.75 to about 4 percent by weight of water and from about 2 to about 8 percent by weight of dibromoneopentyl glycol are used in the polymerization reaction, both percentages being based on the weight of the polyether polyol used in the polymerization reaction.

References Cited (Backward Citations)

US3630973A Cited
US3812047A Cited
US3773696A Cited
US3779953A Cited
US3833665A Cited
US3738953A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-01-19 1979-07-21 1980-01-20 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-01-19 1983-07-21 1984-01-20 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-01-19 1987-07-21 1988-01-20 $7700.00 Window Closed / Lapsed

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