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US4923904A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing polyurethane foam

Assignee: Bridgestone Corp
•
Filing: 1988-12-22
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Granted: 1990-05-08
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Expires: 2008-12-22
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Abstract

Abstract A process for producing a polyurethane foam from a foam raw material containing polyols, organic isocyanates, catalysts and blowing agents, which comprises using as the polyols a high-molecular weight polyol having a hydroxyl number lower than 100 and a low-molecular weight polyol having a hydroxyl number higher than 200 which are mixed at a ratio of 4:6 to 6:4 (by weight), and also using as the catalysts a tertiary amine alone. Polyurethane forms having good buckling performance can be obtained by the process and they are expected to be useful as a packaging material, shock-absorbing material, heat-insulating material, and so on.

Inventors

  • 👤 Hajime Hasegawa
  • 👤 Taiji Koga
  • 👤 Atsuo Takei
  • 👤 Toru Okuyama

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 12:35
CPC Classifications
C; C08; C08G; C08G18/00; C08G18/06; C08G18/08; C08G18/16; C08G18/18; C08G18/20; C08G18/28; C08G18/65; C08G18/66; C08G18/6666; C08G18/667; C08G18/6674; C08G2110/00; C08G2110/0016

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 170 words
A process for producing a polyurethane foam having good buckling performance by a one-shot process or prepolymer process which comprises: mixing a raw material comprising polyols, an organic isocyanate, a catalyst and a blowing agent, said polyols consisting of a mixture of a high-molecular weight polyol having a hydroxyl number of from 25 to 100 and a molecular weight of from 2000 to 4000 and a low-molecular weight polyol having a hydroxyl number of from 200 to 600 and a molecular weight of from 200 to 800 at a weight ratio of 4:6 to 6:4, and said catalyst consisting of a tertiary amine, wherein said organic isocyanate is used in an amount of from 20 to 70 parts by weight for 100 parts by weight of the total amount of said polyols, and said catalyst is used in an amount of from 0.1 to 3 parts by weight for 100 parts by weight of the total amount of said polyols, and foaming said raw material to obtain a polyurethane foam.
Claim 2
Dependent Claim 170 words
A process for producing a polyurethane foam having good buckling performance by a one-shot process or prepolymer process which comprises: mixing a raw material comprising polyols, an organic isocyanate, a catalyst and a blowing agent, said polyols consisting of a mixture of a high-molecular weight polyol having a hydroxyl number of from 25 to 100 and a molecular weight of from 2000 to 4000 and a low-molecular weight polyol having a hydroxyl number of from 200 to 600 and a molecular weight of from 200 to 800 at a weight ratio of 4:6 to 6:4, and said catalyst consisting of a tertiary amine, wherein said organic isocyanate is used in an amount of from 20 to 70 parts by weight for 100 parts by weight of the total amount of said polyols, and said catalyst is used in an amount of from 0.1 to 3 parts by weight for 100 parts by weight of the total amount of said polyols, and foaming said raw material to obtain a polyurethane foam.
Claim 3
Dependent Claim 20 words
The process according to claim 1, wherein the hydroxyl number of the high-molecular weight polyol is from 25 to 60.
Claim 4
Dependent Claim 43 words
The process according to claim 1, wherein the tertiary amine catalyst is selected from the group consisting of triethylenediamine, triethylamine N,N,N',N'-tetra-methyl-1,3-butanediamine, dimethylethanolamine, ethyldiethanolamine, N,N-dimethylcyclohexylamine, N-ethylmorpholine, N-methylmorpholine, 1,8-diazacyclo(5.4.0)undecene-7, bis(2-dimethylamino-ethyl)ether, trimethylaminoethyl piperagine, methylhydroxyethyl piperazin, N,N,N',N'-tetra-methylhexamethylenediamine, N,N,N',N'-tetramethyl-propylenediamine, N,N, N',N',N''-pentamethyl diethylenetriamine, N-trioxyethylene-N,N-dimethyl-amine, N,N,N'-trimethylaminoethyl ethanolamine and mixtures thereof.
Claim 5
Dependent Claim 28 words
The process according to claim 1, wherein the organic isocyanate is selected from the group consisting of m-phenylenediisocyanate, p-phenylenediisocyanate, 2,4-tolylene diisocyanate, 2,6-tolylenediisocyanate, chlorophenylene-2,4-diisocyanate, crude diphenylmethane diisocyanate and mixtures
Claim 6
Dependent Claim 19 words
The process according to claim 1, wherein the raw material further comprises a flame retardant, pigment or inorganic filler.

References Cited (Backward Citations)

US4475847A Cited
US4792576A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1993-05-07 1993-11-06 1994-05-08 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1997-05-07 1997-11-06 1998-05-08 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2001-05-07 2001-11-06 2002-05-08 $7700.00 Window Closed / Lapsed

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