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US5318997A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for production of open cell rigid polyurethane foam

Assignee: Mitsui Chemicals Polyurethanes Inc
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Filing: 1993-04-20
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Granted: 1994-06-07
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Expires: 2013-04-20
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Abstract

Abstract A method of producing an open cell rigid polyurethane foam which comprises reacting a mixture of polyols having a hydroxyl value of 160-360 mg KOH/g with a polyisocyanate in the presence of water as a blowing agent in an amount of 6-12 parts by weight in relation to 100 parts by weight of the mixture of polyols at an isocyanate index of 70-120, the mixture of polyols comprising: (a) 30-60% by weight of a first polyoxyalkylene polyol having a functionality of 2-3.5, a hydroxyl value of 28-90 mg KOH/g, a polyoxyethylene unit content of not more than 5% by weight, and a primary hydroxyl group content of not more than 15% based on the total of the hydroxyl groups of the first polyoxyalkylene polyol; (b) 30-60% by weight of a second polyoxyalkylene polyol having a functionality of 3-6, a hydroxyl value of 150-500 mg KOH/g, and a primary hydroxyl group content of not more than 5% based on the total of the hydroxyl groups of the second polyoxyalkylene polyol; and (c) 0-25% by weight of a third polyol having a functionality of 2-3, a hydroxyl value of 450-840 mg KOH/g, and a primary hydroxyl group content of not more than 5% based on the total of the hydroxyl groups of the third polyol.

Inventors

  • 👤 Kazuo Okada
  • 👤 Yoshihiko Tairaka

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 13:22
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/28; C08G18/65; C08G18/66; C08G18/6666; C08G18/667; C08G18/6681; C08G18/6688; C08G18/40; C08G18/48; C08G18/4804; C08G18/4816; C08G18/482; C08G18/6674; C08G2110/00; C08G2110/0025; C08G2110/0041; C08G2110/005; C08G2110/0083

Claims Analysis

Total Claims: 19
Claim 1
Independent Claim 213 words
A method of producing an open cell rigid polyurethane foam which comprises reacting a mixture of polyols having a hydroxyl value of 160-360 mg KOH/g with a polyisocyanate in the presence of water as a blowing agent in an amount of 6-12 parts by weight in relation to 100 parts by weight of the mixture of polyols at an isocyanate index of 70-120, the mixture of polyols comprising: (a) 30-60% by weight of a first polyoxyalkylene polyol having a functionality of 2-3.5, a hydroxyl value of 28-90 mg KOH/g, a polyoxyethylene unit content of not more than 5% by weight, and a primary hydroxyl group content of not more than 15% based on the total of the hydroxyl groups of the first polyoxyalkylene polyol; (b) 30-60% by weight of a second polyoxyalkylene polyol having a functionality of 3-6, a hydroxyl value of 150-500 mg KOH/g, and a primary hydroxyl group content of not more than 5% based on the total of the hydroxyl groups of the second polyoxyalkylene polyol; and (c) 0-25% by weight of a third polyol having a functionality of 2-3, a hydroxyl value of 450-840 mg KOH/g, and a primary hydroxyl group content of not more than 5% based on the total of the hydroxyl groups of the third polyol.
Claim 2
Independent Claim 213 words
A method of producing an open cell rigid polyurethane foam which comprises reacting a mixture of polyols having a hydroxyl value of 160-360 mg KOH/g with a polyisocyanate in the presence of water as a blowing agent in an amount of 6-12 parts by weight in relation to 100 parts by weight of the mixture of polyols at an isocyanate index of 70-120, the mixture of polyols comprising: (a) 30-60% by weight of a first polyoxyalkylene polyol having a functionality of 2-3.5, a hydroxyl value of 28-90 mg KOH/g, a polyoxyethylene unit content of not more than 5% by weight, and a primary hydroxyl group content of not more than 15% based on the total of the hydroxyl groups of the first polyoxyalkylene polyol; (b) 30-60% by weight of a second polyoxyalkylene polyol having a functionality of 3-6, a hydroxyl value of 150-500 mg KOH/g, and a primary hydroxyl group content of not more than 5% based on the total of the hydroxyl groups of the second polyoxyalkylene polyol; and (c) 0-25% by weight of a third polyol having a functionality of 2-3, a hydroxyl value of 450-840 mg KOH/g, and a primary hydroxyl group content of not more than 5% based on the total of the hydroxyl groups of the third polyol.
Claim 3
Dependent Claim 25 words
The method as claimed in claim 1 wherein the polyol (a) is an addition product of propylene oxide to a polyhydric alcohol as an initiator.
Claim 4
Dependent Claim 29 words
The method as claimed in claim 1 wherein the polyol (b) is an addition product of propylene oxide to an aliphatic amine or an aromatic amine as an initiator.
Claim 5
Dependent Claim 17 words
The method as claimed in claim 1 wherein the polyol (C) is dipropylene glycol or tripropylene glycol.
Claim 6
Dependent Claim 20 words
The method as claimed in claim 1 wherein each of the polyols (a), (b) and (c) is a polyoxypropylene polyol.
Claim 7
Dependent Claim 29 words
The method as claimed in claim 1 wherein the polyisocyanate is polymethylene polyphenyl polyisocyanate having a viscosity of not more than 200 centipoises at the temperature of 25° C.
Claim 8
Dependent Claim 20 words
The method as claimed in claim 1 wherein the mixture of polyols has a hydroxyl value of 250-350 mg KOH/g.
Claim 9
Dependent Claim 23 words
The method as claimed in claim 1 wherein the mixture of polyols is reacted with a polyisocyanate at an isocyanate index of 80-100.
Claim 10
Dependent Claim 35 words
The method as claimed in claim 1 wherein water is used as a blowing agent in an amount of 7-10 parts by weight in relation to 100 parts by weight of the mixture of polyols.
Claim 11
Dependent Claim 20 words
The method as claimed in claim 1 wherein the polyol (a) is an addition product of propylene oxide to glycerine.
Claim 12
Dependent Claim 25 words
The method as claimed in claim 1 wherein the polyol (a) is an addition product of propylene oxide to a mixture of glycerine and methylglucoside.
Claim 13
Dependent Claim 32 words
The method as claimed in claim 1 wherein the polyol (b) is an addition product of propylene oxide to at least one of an ethylene(poly)amine, an aliphatic amine and an aromatic amine.
Claim 14
Dependent Claim 25 words
The method as claimed in claim 1 wherein the polyol (b) is an addition product of propylene oxide to a mixture of sorbitol and glycerine.
Claim 15
Dependent Claim 23 words
The method as claimed in claim 1 wherein the mixture of polyols contains the polyol (a) in an amount of 35-55% by weight.
Claim 16
Dependent Claim 23 words
The method as claimed in claim 1 wherein the mixture of polyols contains the polyol (b) in an amount of 40-55% by weight.
Claim 17
Dependent Claim 23 words
The method as claimed in claim 1 wherein the mixture of polyols contains the polyol (c) in an amount of 0-20% by weight.
Claim 18
Dependent Claim 24 words
The method as claimed in claim 1 wherein when a free foam is produced, the foam has a density of 18-35 kg/m 3 .
Claim 19
Dependent Claim 27 words
The method as claimed in claim 1 wherein when a mold foam or spray foam is produced, the foam has a density of 22-50 kg/m 3 .

References Cited (Backward Citations)

LU68720A1 Cited
US4409341A Cited
JPS6386713A Cited
US4923904A Cited
US5063253A Cited
US5013766A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1997-06-06 1997-12-06 1998-06-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2001-06-06 2001-12-06 2002-06-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2005-06-06 2005-12-06 2006-06-07 $7700.00 Window Closed / Lapsed

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